TWM539991U - Waste disposal and reuse system - Google Patents

Description

Waste treatment and reuse system

This creation is about a waste treatment and reuse system, especially that can process solid waste, liquid waste and hazardous business waste into steam, electricity, molten recycled pellets, high-pressure concrete products or other cement. The system of products.

According to the statistics of the Ministry of Economic Affairs, the annual output value of other domestic cement products has grown from 3.2 billion yuan in 1995 to 5.2 billion yuan in 104 years. Among them, concrete brick products account for more than 50% of the total. It is obvious that concrete bricks are currently One of the commonly used building materials. At present, the main raw materials of concrete bricks include cement, natural pellets (such as sandstone), etc., because sandstone is a natural product, and the sandstones in Taiwan are different due to the geological distribution, and the source rocks are different. Or the quality of the sandstone in the dry season is also different. Therefore, the size distribution and thickness of the grades of the sandstone field are different, which results in unstable sandstone source and quality.

In addition, rapid economic development has led to over-exploitation of natural resources and increasing waste, especially in the textile industry, photovoltaic panel industry and paper industry, etc. The liquid waste generated by the production process and the hazardous business wastes derived from other industries in the production process. In addition to actively promoting the reduction of the source, the government is also committed to recycling waste, and hopes to reduce waste by properly handling the technology. The purpose of the output of matter. In recent years, with the update of public engineering regulations, the chemical composition of iron-making blast furnace stone, fuel-fired power generation fly ash, etc. Industrial process wastes with close proximity to cement are gradually being used to replace natural pellets. Therefore, new types of people can think about how to reduce the demand for environmental natural resources while effectively solving the incinerator fly ash and bottom slag. The final disposal problem can stabilize the quality of raw materials and relieve the dilemma of insufficient energy disposal in domestic waste.

In view of the unstable quality of the main raw materials for the production of concrete bricks at this stage, and the waste processing energy derived from the production process in each business is insufficient, there is still a lack of improvement.

Therefore, the purpose of this creation is to produce solid waste, liquid waste and hazardous industrial waste through solid waste incineration treatment system, liquid waste incineration treatment system and high temperature hot melt treatment system. The dust collection ash is reused as a high-pressure concrete brick or other cement products through the cement product system, and the waste heat energy generated by the waste incineration treatment system can be connected to the steam and electricity symbiosis system to generate steam and electricity, and is used for self-use and factory in the factory. External sales, in order to solve the problem of corporate waste disposal while producing high-pressure concrete bricks or other cement products.

In order to achieve the goal, the present invention provides a waste disposal and reuse system comprising: a solid waste incineration treatment system for treating general business waste including sludge and sludge, the sludge The general business waste is dried into sludge by the sludge drying equipment, and the general business waste except the sludge is crushed by the crushing equipment, pretreated by the separation equipment, and incinerated by the feeding equipment into the solid waste. The equipment is incinerated, and the harmless bottom slag produced after incineration can be crushed by a crusher and used as raw materials for cement products equipment or introduced into high-temperature hot melt processing equipment for incineration, and the waste gas generated after incineration is The first selective non-catalyst reduction denitration system (SNCR), cyclone separator, electrostatic precipitator, first selective catalytic reduction denitration system (SCR), The activated carbon adsorption device, the first bag type dust collector and the washing tower, and the harmful dust collecting ash produced by the electrostatic precipitator and the first bag type dust collector are introduced into the high temperature heat melting processing device to make the treated exhaust gas It is discharged into the atmosphere, and the waste heat passing through the cyclone separator is recovered through the first boiler heat exchange equipment, and the produced high-temperature steam is sent to the steam-electric symbiosis equipment, and is removed by the first selective catalyst. The medium temperature exhaust gas (SCR) and the external air are indirectly heated by the air heating and preheating equipment, and the generated preheated air is sent to the solid waste incineration processing equipment to make the solid waste incineration processing equipment. It can be incinerated by preheated air and external solid, liquid or gaseous fuel; a liquid waste incineration system for treating liquid waste, which is pretreated and then infused into the liquid waste by the feeding equipment. The equipment is incinerated, and the harmful bottom slag generated after incineration is introduced into the high-temperature hot-melt processing equipment, and the exhaust gas generated after incineration is sequentially introduced into the second selective non-contact a reduction denitration system (SNCR), a second selective catalyst reduction denitration system (SCR), an activated carbon adsorption device, a second bag type dust collector, and the washing tower, and the second bag type dust collector is produced The harmful dust collection ash is introduced into the high temperature hot melt processing equipment to discharge the treated exhaust gas to the atmosphere, and the waste heat passing through the second selective non-catalytic reduction denitration system (SNCR) passes through the second boiler heat exchange equipment. Recycling and sending the produced high-temperature steam to the cogeneration plant; a high-temperature hot melt treatment system for treating hazardous business waste, solid waste incineration treatment system and bottom slag of liquid waste incineration treatment system And collecting dust ash, and introducing the molten tail gas into the liquid waste incineration processing device, and the molten material is water quenched to produce molten recycled granules; the oxy-electricity symbiosis system comprises a steam and electricity symbiosis device connected with pure water equipment, Recovering the high temperature steam of the first boiler heat exchange equipment and the second boiler heat exchange equipment, and after being converted into low temperature steam, used for sludge drying equipment, steam health room, and flue gas heater in the plant, and The produced boiler condensate is used for the first boiler heat exchange equipment and the second boiler heat exchange equipment; and a cement product system, the molten material of the high temperature hot melt processing system, and the incineration bottom of the solid waste incineration treatment system Slag After being treated with the refractory material by the masher, the existing raw materials are mixed with the existing raw materials through the cement product equipment, and are subjected to pressure molding, and are processed by the steam health chamber to produce high-pressure concrete products or mixed and then molded to produce Other cement products.

This creation:

1‧‧‧Waste Disposal System

20‧‧‧Solid waste incineration system

200‧‧‧ solid waste incineration equipment

201‧‧‧Sludge storage device

202‧‧‧Sludge drying equipment

203‧‧‧Crushing equipment

204‧‧‧Separation equipment

205‧‧‧Feeding equipment

206‧‧‧First Selective Non-catalytic Reductive Denitration System (SNCR)

207‧‧‧Cyclone separator

208‧‧‧Electrostatic dust collector

209‧‧‧First Selective Catalytic Reduction Denitration System (SCR)

210‧‧‧First bag dust collector

211‧‧‧First boiler heat exchange equipment

212‧‧‧Air heating preheating equipment

213‧‧·washing tower

30‧‧‧Liquid waste incineration system

300‧‧‧Liquid waste incineration equipment

301‧‧‧ Waste solvent storage device

302‧‧‧Feeding equipment

303‧‧‧Second selective non-catalytic reduction denitration system (SNCR)

304‧‧‧Second boiler heat exchange equipment

305‧‧‧Second selective catalytic reduction denitration system (SCR)

306‧‧‧Second bag dust collector

40‧‧‧High temperature hot melt processing system

400‧‧‧High temperature hot melt processing equipment

50‧‧‧Automotive symbiosis system

500‧‧‧Vapor symbiosis equipment

501‧‧‧ pure water equipment

502‧‧‧Fume gas heater

60‧‧‧Cement products system

600‧‧‧Cement products equipment

601‧‧‧masher

602‧‧‧Steam Health Room

A‧‧‧ solid waste

A-1‧‧‧General business waste (sludge)

A-1-1‧‧‧dry sludge

A-1-2‧‧‧ Wet sludge

A-2‧‧‧General business waste (excluding sludge)

B‧‧‧Liquid waste

C‧‧‧Hazardous waste

D-1‧‧‧ harmless bottom slag

D-2‧‧‧ harmful bottom slag

F‧‧‧Active carbon adsorption equipment

G‧‧‧Steam

H‧‧‧Air

I-1‧‧‧solid, liquid or gaseous fuel

I-2‧‧‧Liquid or gaseous fuel

J-1‧‧‧Innocent dust collection ash

J-2‧‧‧Hazardous dust ash

K‧‧‧Molten exhaust

L‧‧‧Molten recycled pellets

M‧‧‧Power

O‧‧‧ tap water

P‧‧‧Condensate

Q‧‧‧Waste refractory

R‧‧‧ Existing raw materials

S‧‧‧High-pressure concrete products or other cement products

T‧‧‧ melt

Figure 1 is an architectural diagram of the authoring system.

Figure 2 is a flow chart of the authoring system.

In order to make your reviewers understand the techniques, means and functions used in the purpose of this creation, the rest of the examples are illustrated with a detailed description of the following: First, please refer to Figure 1 with the second As shown, the waste treatment recycling system 1 comprises a solid waste incineration treatment system 20, a liquid waste incineration treatment system 30, a high temperature heat fusion treatment system 40, a steam and electricity symbiosis system 50, and a cement product system. 60. The solid waste incineration treatment system 20 is used to treat general waste (sludge) A-1 of solid waste A and general business waste (excluding sludge) A-2, and is connected to high temperature hot melt. The treatment system 40, the cogeneration system 50 and the cement product system 60. In one embodiment of the present invention, the general business waste (sludge) A-1 contains organic sludge, inorganic sludge, and is not harmful. One or a combination of sludge, sludge mixture, pulp sludge, and textile sludge, general business waste (excluding sludge) A-2 contains waste ion exchange resin, solid waste resin other than waste ion exchange resin, Waste plastic mixture, waste rubber mixture, waste wood pallet, waste wood mixture, other general business waste, waste dust collector filter bag, general garbage, or a combination thereof; liquid waste incineration treatment system 30 For treating the liquid waste B, and connecting to the high-temperature heat-melting treatment system 40 and the steam-electricity symbiosis system 50, in one embodiment of the present invention, the liquid waste B contains waste resin other than the waste ion exchange resin, Harmful organic waste liquid or waste solvent, non-hazardous mixed waste liquid, waste oil mixture, general chemical substance, waste medicine, arsenic and compound (total arsenic), other corrosive business waste mixture, waste liquid flash point less than 60 °C (excluding alcohol waste with an ethanol concentration less than 24%), or other combustible business waste mixture, or a combination thereof; high temperature hot melt processing system 40 for treating hazardous business waste C and solid waste incineration The bottom slag and dust ash generated by the treatment system 20 and the liquid waste incineration treatment system 30 are treated in one embodiment of the present invention, and the hazardous business waste C includes the use of a heat treatment method to treat hazardous business waste. Dust ash, residue or sludge from waste recycling, wastewater treatment sludge for electroplating process, does not contain aluminum sulfuric acid plating, carbon steel tin plating, carbon steel aluminizing, accompanying cleaning or stripping Produced by steel tin, aluminum, aluminum etching and grinding processes, other chemical mixtures or waste containers, arsenic and its compounds (total arsenic), copper and its compounds (total copper) (disposable catalysts, sets only) Dust, waste, sludge, filter, incinerated fly ash or bottom slag), other mixed waste containing toxic heavy metals and exceeding the dissolution standard.

Next, please refer to the first to second figures, the general business waste (sludge) A-1 of the solid waste A is stored in the sludge storage device 201, wherein the wet sludge A-1-2 is required. First, the sludge drying equipment 202 is heated by steam to dry the dry sludge A-1-1 having a water content of less than 60%, and the general commercial waste (excluding sludge) A-2 is first processed into the crushing equipment 203. Thereafter, dry sludge A-1-1 and general commercial waste (excluding sludge) A-2 are introduced into separation equipment 204 for pretreatment, and are fed into solid waste incineration treatment equipment 200 by charging equipment 205 for incineration. In one embodiment, the solid waste incineration treatment equipment 200 is a general incinerator, a cyclone incinerator, a vertical fluidized bed furnace, a horizontal fluidized bed furnace or a cyclone fluidized bed furnace; The harmless bottom slag D-1 produced after incineration is introduced into the high temperature hot melt processing equipment 400 or passed through the masher 601 and introduced into the cement product equipment 600. The waste gas produced after incineration contains heavy metals such as granules, sulfur oxides, nitrogen oxides, lead, cadmium and mercury, and dioxin, so it is necessary to enter the first selective non-catalytic reduction denitration system (SNCR) 206 in sequence. a cyclone separator 207, an electrostatic precipitator 208, a first selective catalytic reduction denitration system (SCR) 209, a first baghouse 210 and a scrubber 213 for passing the exhaust gas through the first selective non-contact After the medium reduction denitration system (SNCR) 206 converts nitrogen oxides into nitrogen and water, the cyclone separator 207 and the electrostatic precipitator 208 are used to remove granular contaminants of different particle sizes, and the harmless dust collection ash J- 1 (harmless high temperature ash) according to its needs, can be introduced into the high temperature hot melt processing equipment 400 to melt or become the raw material required for the cement product equipment 600, and the remaining exhaust gas passes through the first selective catalyst reduction denitration system (SCR) 209 By catalytic catalyst, the nitrogen oxides in the exhaust gas are again converted into nitrogen and water, and passed through an activated carbon adsorption device F, such as a fixed adsorption bed, a spray device, etc., to adsorb the dioxin and other compounds in the exhaust gas, and then Through the first bag dust collector 210 The adsorbed activated carbon is collected by filtration, and the harmful dust ash J-2 (harmful low temperature ash) is introduced into the high temperature hot melt processing equipment 400 for incineration, and the remaining harmless exhaust gas is subjected to desulfurization washing treatment by the liquid alkali through the washing tower 213. The exhaust gas is discharged to the atmosphere, and the washing tower 213 wastewater is disposed of through the wastewater treatment equipment. In addition, a first boiler heat exchange device 211 is disposed between the cyclone separator 207 and the electrostatic precipitator 208, and the first selective catalyst reduction denitration system (SCR) 209 and the first baghouse 210 An air heating preheating device 212 is disposed between the cyclone separator 207 to recover the heat of the waste heat through the first boiler heat exchange device 211, and the produced high temperature steam G is sent to the steam cogeneration device. 500, while the external air H can be indirectly heated by the air heating preheating device 212, and the preheated air produced is The gas H is sent to the solid waste incineration treatment device 200, so that the solid waste incineration treatment device 200 can use the preheated air H and the external solid, liquid or gaseous fuel I-1 as the combustion energy.

The liquid waste B is stored in the waste solvent storage device 301, and is incinerated by the feeding device 302 into the liquid waste incineration treatment device 300 after pretreatment, and the harmful bottom slag D-2 generated after incineration is introduced into the high The warm-melt processing apparatus 400 is burned because the liquid waste incineration processing apparatus 300 is an external liquid or gaseous fuel I-2, external air H, volatile gas or odor gas extracted from the waste solvent storage device 301, and high-temperature heat melting. The molten tail gas K of the processing equipment 400 is a combustion energy source. Therefore, the exhaust gas contains heavy metals such as granules, sulfur oxides, nitrogen oxides, lead, cadmium, mercury, and dioxin, so the exhaust gas generated after incineration needs to enter the first step. A selective non-catalytic reduction denitration system (SNCR) 303, a second boiler heat exchange device 304, a second selective catalytic reduction denitration system (SCR) 305, a second baghouse 306, and a scrubber 213 Exhaust gas is subjected to preliminary denitration operation through a second selective non-catalyst reduction denitration system (SNCR) 303, and waste heat recovery is performed through the second boiler heat exchange device 304 to reduce the exhaust gas temperature, and then the produced gas is produced. The warm steam G is sent to the steam-electricity symbiosis device 500, and then, the second selective catalyst reduction sodium reduction system (SCR) 305 is used to reduce the nitrogen oxides by ammonia catalysis by the catalytic action of the catalyst, and the exhaust gas after denitration is activated. The carbon adsorption device F, such as a fixed adsorption bed, a spray device, or the like, adsorbs the dioxin and other compounds in the exhaust gas, and then collects and collects the adsorbed activated carbon through the second bag type dust collector 306, and then removes the harmful dust. Ash J-2 (harmful low temperature ash) is introduced into the high temperature hot melt processing equipment 400 for combustion, and the remaining harmless exhaust gas is subjected to desulfurization washing treatment by the liquid alkali through the washing tower 213, so that the exhaust gas can be discharged to the atmosphere through the chimney, and the washing tower 213 wastewater is disposed of through wastewater treatment equipment.

The hazardous business waste C is processed by the high-temperature heat-melting processing apparatus 400. In one embodiment of the present invention, the high-temperature hot-melt processing apparatus 400 is an electric arc furnace, a plasma melting furnace, One or a combination of a resistance melting furnace, a induced electric heating melting furnace, a rotary surface melting furnace, an internal combustion type fixed surface melting furnace, a rotary reflux melting furnace, a coke bed vertical kiln internal melting furnace, and a high temperature The hot melt processing system 40 uses a high-temperature melting technique to crack the organic matter contained in the waste into a small molecule gas in an oxygen-free operating environment, and then introduces the molten tail gas K generated during the operation into the liquid waste incineration processing device. 300 is subjected to aerobic combustion to remove chemical toxicity, and the inorganic matter contained in the melt T after the waste treatment is introduced into the masher 601, and the other portion is melted into a liquid state, and then converted into lava and discharged in the slurry. The water quenching method is used to produce the vitrified water quenching and regenerating pellet L, and the molten reclaimed pellet L can be directly sold as a commodity outside the factory, or introduced into the in-plant cement product equipment 600 for high-pressure concrete products or other cement products. Process use.

The cogeneration system 50 includes a steam and electricity symbiosis device 500 coupled with a pure water device 501. In addition to recovering the high temperature steam G of the first boiler heat exchange device 211 and the second boiler heat exchange device 304, it can also be converted into high temperature steam G. After the low-temperature steam G, the product is directly sold outside the factory, or imported into the plant for use in the sludge drying equipment 202, the steam health room 602, the flue gas heater 502, and at the same time, it can be sold outside the factory or provided in the factory. The power M used by the system and the boiler condensate P produced by the steam-electricity symbiosis device 500 are used by the first boiler heat exchange device 211 and the second boiler heat exchange device 304. The pure water equipment 501 is produced by external tap water O, clean steam condensed water P produced by the sludge drying equipment 202, and low temperature steam G produced by the steam-electricity symbiosis apparatus 500 after being heated by the flue gas heater 502. The steam condensate P is the source of supply.

The molten material T treated by the high-temperature hot-melt processing apparatus 400 and the harmless bottom slag D-1 and the waste refractory material Q incinerated by the solid waste incineration processing equipment 200 can be processed into the cement product after being processed by the masher 601. System 60, the cement product equipment 600 is added to the existing raw materials R (such as cement, natural pellets, toner, non-hazardous waste dust or mixtures thereof, etc.) and water, blending After the ratio, the mixture is mixed and molded into a mold, and is processed by the steam curing room 602 to produce high-pressure concrete products, or mixed and then molded to produce other cement products, wherein the high-pressure concrete products include interlocking high-pressure floor tiles, Planting bricks, hollow bricks, continental ordinary bricks, floor tiles and blocks, etc., while other cement products include plates, tiles, pipes, boxes, and wave-blocking blocks, etc., for fences, waterfronts or slopes, Use in parking lot areas, pedestrian or car dealers, kerchiefs, wave blocks, sewage pipes, etc.

Therefore, using the waste disposal and reuse system of this creation can obviously achieve the following effects:

1. The waste disposal and reuse system of this creation processes solid waste and liquid waste through solid waste incineration treatment system and liquid waste incineration treatment system, and uses high temperature heat fusion treatment system to treat hazardous business waste. The harmful or harmless bottom slag and the dust-collecting ash produced by solid waste and liquid waste after incineration to produce molten recycled pellets, and the molten recycled pellets can be directly sold as products outside the factory, or through cement products. The system processes and produces high-pressure concrete products or other cement products, thereby solving the problem of enterprise waste disposal and producing molten recycled pellets, high-pressure concrete products or other cement products that can be directly sold outside the factory, thereby achieving waste resources. The effect of the transformation.

2. The waste disposal and reuse system of the present invention recovers the high-temperature steam produced by the solid waste incineration treatment system and the liquid waste incineration treatment system by setting up the steam and electricity symbiosis system, and converts it into steam required for the in-plant process. At the same time, it produces electricity that can be used by various systems in the plant, and can sell steam and electricity to reduce the cost of manufacturing.

3. The waste disposal and reuse system of this creation processes solid waste, liquid waste and hazardous industrial waste to produce molten recycled pellets, so it can replace some natural pellets and reduce the demand for environmental natural resources. Quantity and hazard.

However, the above descriptions are only preferred embodiments of the present invention, and are not intended to limit the scope of implementation of the present invention. Any changes and modifications that do not depart from the spirit of the present invention are covered by the scope of the present invention.

In summary, this creation has indeed broken through the tradition and has improved and innovative creation content and can be specifically implemented. It should meet the statutory requirements of the new patent, and file a patent application according to law, and invite the examination committee of the bureau to grant legal patent rights. Creation, to the sense of virtue.

1‧‧‧Waste Disposal System

200‧‧‧ solid waste incineration equipment

201‧‧‧Sludge storage device

202‧‧‧Sludge drying equipment

203‧‧‧Crushing equipment

204‧‧‧Separation equipment

205‧‧‧Feeding equipment

206‧‧‧First Selective Non-catalytic Reductive Denitration System (SNCR)

207‧‧‧Cyclone separator

208‧‧‧Electrostatic dust collector

209‧‧‧First Selective Catalytic Reduction Denitration System (SCR)

210‧‧‧First bag dust collector

211‧‧‧First boiler heat exchange equipment

212‧‧‧Air heating preheating equipment

213‧‧·washing tower

300‧‧‧Liquid waste incineration equipment

301‧‧‧ Waste solvent storage device

302‧‧‧Feeding equipment

303‧‧‧Second selective non-catalytic reduction denitration system (SNCR)

304‧‧‧Second boiler heat exchange equipment

305‧‧‧Second selective catalytic reduction denitration system (SCR)

306‧‧‧Second bag dust collector

400‧‧‧High temperature hot melt processing equipment

500‧‧‧Vapor symbiosis equipment

501‧‧‧ pure water equipment

502‧‧‧Fume gas heater

600‧‧‧Cement products equipment

601‧‧‧masher

602‧‧‧Steam Health Room

A‧‧‧ solid waste

A-1‧‧‧General business waste (sludge)

A-1-1‧‧‧dry sludge

A-1-2‧‧‧ Wet sludge

A-2‧‧‧General business waste (excluding sludge)

B‧‧‧Liquid waste

C‧‧‧Hazardous waste

D-1‧‧‧ harmless bottom slag

D-2‧‧‧ harmful bottom slag

F‧‧‧Active carbon adsorption equipment

G‧‧‧Steam

H‧‧‧Air

I-1‧‧‧solid, liquid or gaseous fuel

I-2‧‧‧Liquid or gaseous fuel

J-1‧‧‧Innocent dust collection ash

J-2‧‧‧Hazardous dust ash

K‧‧‧Molten exhaust

L‧‧‧Molten recycled pellets

M‧‧‧Power

O‧‧‧ tap water

P‧‧‧Condensate

Q‧‧‧Waste refractory

R‧‧‧ Existing raw materials

S‧‧‧High-pressure concrete products or other cement products

T‧‧‧ melt

Claims (12)

A waste disposal and reuse system comprising: a solid waste incineration treatment system coupled to a high temperature hot melt treatment system, a steam and electricity symbiosis system, and a cement product system to separately treat the solid waste incineration treatment system after incineration a bottom liquid slag, high temperature steam and dust collecting ash; a liquid waste incineration treatment system coupled to the high temperature hot melt processing system and the steam and electricity symbiosis system to treat the bottom generated by the liquid waste incineration treatment system after incineration a high temperature hot melt processing system coupled to the solid waste incineration treatment system, the liquid waste incineration treatment system, and the cement product system for melting the bottom slag and the dust collection ash and providing the same a raw material for a cement product system; a first-gas symbiosis system coupled to the solid waste incineration treatment system, the liquid waste incineration treatment system, and the cement product system for recovering and converting the solid waste incineration treatment system and the liquid The high temperature steam produced by the waste incineration treatment system and the power required for the cement product system And a cement product system coupled to the solid waste incineration treatment system, the high temperature heat fusion treatment system, and the steam and electricity symbiosis system for producing high pressure concrete products or other cement products. The waste disposal and recycling system according to claim 1, wherein the solid waste incineration treatment system is for treating general commercial waste including sludge and sludge, and the solid waste incineration treatment system comprises Solid waste incineration treatment equipment, sludge storage device, crushing equipment, separation equipment, feeding equipment, cyclone separator, first boiler heat exchange equipment, electrostatic precipitator, air heating preheating equipment, first bag set Dust collector and washing tower. The waste disposal and reuse system according to claim 2, wherein the sludge general business waste comprises organic sludge, inorganic sludge, non-hazardous sludge, sludge mixture, pulp sludge, textile stain Mud one or a combination thereof, and the general business waste except the sludge includes waste ion exchange resin, solid waste resin other than waste ion exchange resin, waste plastic mixture, waste rubber mixture, waste wood pallet, waste wood Mixture, other general business waste, waste dust collector filter bag, general waste, or a combination thereof. The waste disposal and reuse system according to claim 1, wherein the solid waste incineration treatment device is a general incinerator, a cyclone incinerator, a vertical fluidized bed furnace, a horizontal fluidized bed furnace or a cyclone type. Fluidized bed furnace. The waste disposal and reuse system according to claim 1, wherein the liquid waste incineration treatment system is for treating liquid waste, and the liquid waste incineration treatment system comprises a liquid waste incineration treatment device and a waste solvent storage device. , feeding equipment, second boiler heat exchange equipment, second bag dust collector and washing tower. The waste disposal and reuse system according to claim 5, wherein the liquid waste comprises waste resin other than waste ion exchange resin, non-hazardous organic waste liquid or waste solvent, non-harmful mixed waste liquid, waste oil mixture , general chemical substances, waste drugs, arsenic and compounds (total arsenic), other corrosive business waste mixtures, waste flash point less than 60 ° C (excluding alcohol waste with less than 24% ethanol concentration), other flammable One or a combination of a commercial waste mixture. The waste treatment recycling system according to claim 1, wherein the high temperature heat fusion treatment system is for treating hazardous business waste, the solid waste incineration treatment system, and the bottom slag of the liquid waste incineration treatment system. The dust ash is collected, and the high temperature hot melt processing system includes a high temperature hot melt processing device. The waste disposal and reuse system according to claim 7, wherein the high temperature hot melt processing equipment is an electric arc furnace, a plasma melting furnace, a resistance melting furnace, a induction heating melting furnace, a rotary surface melting furnace, and an internal combustion type fixing. One or a combination of a surface melting furnace, a rotary reflux melting furnace, a coke bed vertical kiln internal melting furnace. The waste disposal and reuse system according to claim 7, wherein the hazardous business waste includes waste dust generated by using a heat treatment method to treat hazardous business waste, residue or sludge generated by waste recovery, and wastewater of an electroplating process. Treatment of sludge, not including aluminum sulfuric acid plating, carbon steel tin plating, carbon steel aluminizing, carbon steel tin plating with cleaning or stripping, aluminum and aluminum etching and grinding processes, other chemical mixtures or Waste containers, arsenic and its compounds (total arsenic), copper and its compounds (total copper) (for waste catalysts, dust ash, waste liquid, sludge, filter media, incineration fly ash or bottom slag), others containing poison Mixed waste that is heavy metal and exceeds the dissolution standard. The waste disposal and reuse system according to claim 1, wherein the steam and electricity symbiosis system comprises a steam and electricity symbiosis device coupled with a pure water device and a flue gas heater. The waste treatment recycling system of claim 1, wherein the cement product system comprises a cement product equipment, a masher, and a steam health room. The waste disposal and reuse system according to claim 1, wherein the high-pressure concrete product comprises interlocking high-pressure floor tiles, grass bricks, hollow bricks, continental ordinary bricks, floor tiles and blocks, and the other cement products comprise plates, tiles, tubes, Box and wave block.