CN108826318A - Domestic garbage treating system and life refuse processing method - Google Patents

Domestic garbage treating system and life refuse processing method Download PDF

Info

Publication number
CN108826318A
CN108826318A CN201810763719.9A CN201810763719A CN108826318A CN 108826318 A CN108826318 A CN 108826318A CN 201810763719 A CN201810763719 A CN 201810763719A CN 108826318 A CN108826318 A CN 108826318A
Authority
CN
China
Prior art keywords
gas
flue gas
solid
outlet
sent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810763719.9A
Other languages
Chinese (zh)
Inventor
龙潭
王尚文
闫金银
马尊领
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Qiyao Thermal Engineering Co Ltd
Shanghai Marine Diesel Engine Research Institute
711th Research Institute of CSIC
Original Assignee
Shanghai Qiyao Thermal Engineering Co Ltd
711th Research Institute of CSIC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shanghai Qiyao Thermal Engineering Co Ltd, 711th Research Institute of CSIC filed Critical Shanghai Qiyao Thermal Engineering Co Ltd
Priority to CN201810763719.9A priority Critical patent/CN108826318A/en
Publication of CN108826318A publication Critical patent/CN108826318A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/033Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L15/00Heating of air supplied for combustion
    • F23L15/04Arrangements of recuperators
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

The present invention provides a kind of domestic garbage treating system and life refuse processing methods.The system includes pretreatment unit, incinerator, flue gas separation unit, flue gas purification device and plasma gasification cracking melting plant.The pretreating waste outlet of pretreatment unit is connected with the pretreating waste import of incinerator;The gas inlet of the gas-solid separator of the high-temperature flue gas outlet and flue gas separation unit of incinerator is connected;First waste gas outlet of gas-solid separator is connected with the first exhaust gas entrance of flue gas purification device;Plasma gasification cracking melting plant includes interconnected plasma gasification cracking melting furnace and molten slag discharge quenching apparatus, and the flying dust outlet of gas-solid separator and the first solid residue outlet of incinerator are connected with the plasma furnace solid waste feed inlet of plasma gasification cracking melting furnace.The gaseous effluent ingredient of generation cleans, and will not cause secondary pollution to atmosphere;The solid product of generation can be secondary use.

Description

Domestic garbage treating system and life refuse processing method
Technical field
The present invention relates to field of garbage disposal, and relate more specifically at a kind of domestic garbage treating system and house refuse Reason method.
Background technique
Since China's domestic waste is by the way of mixed collection, rubbish constituent is complicated, including kitchen waste material, modeling Material, rubber, stationery, wood bamboo, fabric, glass, metal etc., the characteristics such as each component particle size, hardness, moisture content are different, such as food waste Water content of matter is high, and light plastic is difficult to broken etc., leads to the increase of its processing difficulty.
Currently, the main processing ways of domestic rubbish have:(1) landfill method, the percolate and foul smell that this method generates Seriously polluted, landfill area easily causes soil and groundwater to pollute;(2) incineration method, can generate in this method treatment process largely has Evil gas, the flying dust for burning generation do not dispose properly, can cause environmental pollution and air pollution.In above-mentioned technology, to life Rubbish living can not achieve harmless treatment, cannot be recycled to part house refuse, and will cause environmental pollution and sky Gas pollution.
Therefore, it is necessary to a kind of domestic garbage treating systems and a kind of life refuse processing method, at least to be partially solved Problems of the prior art.
Summary of the invention
A series of concept of reduced forms is introduced in Summary, this will in the detailed description section into One step is described in detail.Summary of the invention is not meant to attempt to limit technical solution claimed Key feature and essential features do not mean that the protection scope for attempting to determine technical solution claimed more.
In order at least be partially solved the above problem, according to an aspect of the invention, there is provided at a kind of house refuse Reason system comprising:
Pretreatment unit, the pretreatment unit include house refuse import and pretreating waste outlet;
Incinerator, the incinerator include pretreating waste import, high-temperature flue gas outlet and the outlet of the first solid residue, institute Pretreating waste import is stated to be connected with pretreating waste outlet;
Flue gas separation unit, the flue gas separation unit include gas-solid separator, the gas-solid separator include flue gas into Mouth, flying dust outlet and the first waste gas outlet, the gas inlet are connected with the high-temperature flue gas outlet;
Flue gas purification device, the flue gas purification device include that the first exhaust gas entrance and gaseous effluent export, and described the One exhaust gas entrance is connected with first waste gas outlet;And
Plasma gasification cracks melting plant, and plasma gasification cracking melting plant includes interconnected etc. Gas ions gasification cracking melting furnace and molten slag discharge quenching apparatus, the plasma gasification cracking melting furnace include it is equal from Daughter furnace solid waste feed inlet, the plasma furnace solid waste feed inlet is exported with the flying dust and first solid residue goes out Mouth connection, the molten slag discharge quenching apparatus are connected to slag collector.
After domestic garbage treating system according to the present invention is to domestic rubbish disposal, on the one hand, the gaseous effluent of generation Ingredient cleaning, secondary pollution will not be caused to atmosphere after discharge;On the other hand, the solid product volume of generation is smaller, more pacifies Entirely, it can be secondary use, be truly realized " innoxious, minimizing, recycling ".
Optionally, the flue gas separation unit further includes air preheater, and the air preheater includes:
High-temperature flue gas entry, the high-temperature flue gas entry are connected with the high-temperature flue gas outlet;
Low-temperature flue gas outlet, the low-temperature flue gas outlet are connected with the gas inlet;
First cool air inlet, first cool air inlet is for being passed through cold air into the air preheater;With And
Hot air outlet.
Optionally, the plasma gasification cracking melting furnace further includes reducibility gas outlet, and the incinerator includes Reducibility gas entrance, the reducibility gas outlet are connected to the reducibility gas entrance.
Optionally, the pretreatment unit includes crusher and drying device, and the crusher includes house refuse import It is exported with house refuse is crushed, the drying device includes crushing house refuse import and pretreating waste outlet, the crushing House refuse outlet is connected with the crushing house refuse import.
Optionally, the drying device includes the first hot air inlet, and the plasma gasification cracking melting furnace includes Second hot air inlet, first hot air inlet and second hot air inlet are connected to the hot air outlet.
Optionally, the drying device further includes the second cold-air vent, and the incinerator includes the second cool air inlet, Second cold-air vent is connected to second cool air inlet.
Optionally, it is set between the plasma gasification cracking melting furnace and the gas-solid separator and the incinerator Set solid resultant product collection device, the solid resultant product collection device includes the second solid waste feed inlet and the second solid waste discharge port, and described the Two solid waste feed inlets are exported with the flying dust and first solid residue outlet is connected, the second solid waste discharge port and institute Plasma furnace solid waste feed inlet is stated to be connected.
According to another aspect of the present invention, a kind of life refuse processing method is provided, is included the following steps:
House refuse is sent into pretreatment unit and carries out pre-treatment step, obtains pretreating waste;
The pretreating waste is sent into incinerator to burn, obtains high-temperature flue gas and the first solid residue;
The high-temperature flue gas is sent into gas-solid separator, obtains the first exhaust gas and flying dust;
First exhaust gas is sent into flue gas purification device, obtains the gaseous effluent for capableing of direct emission;And
First solid residue and the flying dust are sent into plasma gasification and crack melting furnace, obtains molten product, The molten product is sent into molten slag discharge quenching apparatus and carries out quenching, obtains glassy particles.
When life refuse processing method processing house refuse according to the present invention, on the one hand, the gaseous effluent of generation Ingredient cleaning, will not cause secondary pollution to atmosphere after discharge;On the other hand, the solid product volume of generation is smaller, safer, It can be secondary use, be truly realized " innoxious, minimizing, recycling ".
Optionally, the life refuse processing method is further comprising the steps of:
The high-temperature flue gas and cold air are sent into air preheater, so that the high-temperature flue gas and the cold air are in institute It states in air preheater and exchanges heat, obtain low-temperature flue gas and hot-air;And
The low-temperature flue gas is sent into the gas-solid separator, the hot-air is sent into the pretreatment unit and described Plasma gasification cracks melting furnace.
Optionally, the life refuse processing method is further comprising the steps of:
The hot-air exchanges heat in the pretreatment unit, obtains the second cold air, by second cold air It is sent into the incinerator.
Optionally, the flying dust and first solid residue are sent into solid resultant product collection device, the flying dust and described First solid residue is sent into the plasma gasification cracking melting furnace after assembling in the solid resultant product collection device.
Optionally, generating in the plasma gasification cracking melting furnace has reducibility gas, by the reducibility gas It is sent into the incinerator.
Optionally, the pre-treatment step includes:
The house refuse is sent into broken crusher machine, obtains broken house refuse;And
The broken house refuse is sent into the drying device drying, obtains pretreating waste.
Detailed description of the invention
Following drawings of the invention is incorporated herein as part of the present invention for the purpose of understanding the present invention.Shown in the drawings of this hair Bright embodiment and its description, device used to explain the present invention and principle.In the accompanying drawings,
Fig. 1 is the structural schematic diagram according to the domestic garbage treating system of an embodiment of the invention.
Description of symbols:
110:House refuse 121:Drying device
122:Crusher 130:Incinerator
141:Gas-solid separator 142:Air preheater
143:Flue gas purification device 144:Air blower
145:Chimney 146:Solid resultant product collection device
151:Plasma gasification cracks melting furnace 152:Molten slag discharges quenching apparatus
153:Slag collector 160:Construction material
Q1:High-temperature flue gas Q2:Cold air
Q3:Hot-air Q4:Low-temperature flue gas
Q5:Second cold air Q6:Reducibility gas
Q7:First exhaust gas
Specific embodiment
In the following description, a large amount of concrete details are given so as to provide a more thorough understanding of the present invention.So And it is obvious to the skilled person that the present invention may not need one or more of these details and be able to Implement.In other examples, in order to avoid confusion with the present invention, for some technical characteristics well known in the art not into Row description.
In order to thoroughly understand the present invention, detailed structure will be proposed in following description, to illustrate the present invention.It is aobvious So, execution of the invention is not limited to the specific details that the those skilled in the art are familiar with.Preferable reality of the invention Example is applied to be described in detail as follows, however other than these detailed descriptions, the present invention can also have other embodiments, should not solve It is interpreted as being confined to embodiments presented herein.
The cited such as ordinal number of " first " and " second " is only to identify in the present invention, without any other Meaning, such as specific sequence etc..Moreover, for example, term " first component " itself does not imply that the presence of " second component ", art Language " second component " does not imply that the presence of " first component " in itself.
Hereinafter, specific embodiments of the present invention are described in more detail with reference to the accompanying drawings, shown in the drawings of this hair Bright representative embodiment is not to limit the present invention.
According to an aspect of the invention, there is provided a kind of domestic garbage treating system.As shown in Figure 1, the house refuse Processing system 100 mainly includes pretreatment unit, incinerator 130, flue gas separation unit, flue gas purification device 143 and plasma Body gasification cracking melting plant.The various pieces of domestic garbage treating system 100 according to the present invention are described more fully below.
Pretreatment unit includes house refuse import and pretreating waste outlet.House refuse 110 by house refuse into Mouth is sent into pretreatment unit, to carry out for example dry pretreatment operation, by advance after pre-processing to house refuse Handle garbage outlet discharge.As shown in Figure 1, pretreatment unit may include crusher 122 and drying device 121.
Crusher 122 may include above-mentioned house refuse import and crush house refuse outlet.Drying device 121 includes House refuse import and above-mentioned pretreating waste outlet are crushed, house refuse outlet and the crushing house refuse import are crushed It is connected.For example, the house refuses 110 such as native stone, glass, battery, metal for being collected into can be broken in crusher 122, with After can be delivered to drying device 121 by tools such as belts, the garbage drying after sufficiently dry goes out from pretreating waste Mouth discharge drying device 121.Drying temperature in drying device 121 can be about 300 DEG C.
Incinerator 130 includes pretreating waste import, high-temperature flue gas outlet and the outlet of the first solid residue.Incinerator 130 The pretreating waste outlet of pretreating waste import and drying device 121 be connected.Drying rubbish after drying device 121 is dry Rubbish enters incinerator 130 from pretreating waste import, to carry out burning disposal.Incineration temperature in incinerator 130 can be 900-1000℃.Wherein, before garbage drying is put into incinerator 130, incinerator 300 can be preheated using burner 131 To 600 DEG C.Optionally, garbage drying can be thrown in incinerator 130 via feeder (not shown).Garbage drying is burning It is burned in furnace 130, obtains high-temperature flue gas Q1 and the first solid product.Wherein, the temperature of high-temperature flue gas Q1 is about 800 DEG C;First Solid product can be the incombustible substances such as metal and its oxide, coke, glass in biochemical rubbish.
Flue gas separation unit includes gas-solid separator 141.Gas-solid separator 141 includes gas inlet, flying dust outlet and the One waste gas outlet.Wherein, the gas inlet of gas-solid separator 141 is connected with the high-temperature flue gas outlet of incinerator 130.Garbage drying The high-temperature flue gas Q1 obtained after being incinerated can enter gas-solid separator 141 by gas inlet, in separating high-temp flue gas Q1 The first exhaust gas Q7 and flying dust.
Flue gas purification device 143 includes that the first exhaust gas entrance and gaseous effluent export.The first of flue gas purification device 143 Exhaust gas entrance is connected with the first waste gas outlet of gas-solid separator 141.First exhaust gas Q7 is sent into flue gas by the first exhaust gas entrance Purification device 143.Flue gas purification device 143 carries out the processes such as desulphurization and denitration to the first exhaust gas Q7, obtains to atmospheric environment without dirt Gaseous effluent dye, being capable of direct emission.Optionally, domestic garbage treating system 100 according to the present invention can also wrap Include chimney 145.Chimney 145 is configured to the gaseous effluent outlet of connection flue gas purification device 143.Gaseous effluent can be via Gaseous effluent outlet enters chimney 145, and is emitted into atmosphere by chimney 145.
Plasma gasification cracking melting plant includes interconnected plasma gasification cracking melting furnace 151 and liquid Slag discharge quenching apparatus 152.It includes plasma furnace solid waste feed inlet that plasma gasification, which cracks melting furnace 151,.Plasma First solid residue outlet of the outlet of the flying dust of body furnace solid waste feed inlet and gas-solid separator 141 and incinerator 130.By This, the flying dust isolated in the first solid product and high-temperature flue gas Q1 that garbage drying obtains after being incinerated can pass through plasma Body furnace solid waste feed inlet is sent into plasma gasification and cracks melting furnace 151, with the quilt in plasma gasification cracking melting furnace 151 Liquefaction melting.Plasma gasification cracks and is provided with plasma gun 154 in melting furnace 151, and plasma gun 154 can be etc. Gas ions gasification cracking melting furnace 151 provides about 1600 DEG C of high temperature.
Plasma gasification under about 1400 DEG C, the plasma atmosphere of high reaction activity and low-oxygen environment cracks melting In furnace 151, the combustible component in solid waste generates reducibility gas Q6, and non-combustible ingredient generates molten product.Reproducibility gas Body Q6 can be CO, H2.For example, the organic matter in solid waste generates CO, H by gasification cracking2Equal reducibility gas;Metal oxygen Compound is reduced generation metal simple-substance;The inorganic salts such as silicate generate the substances such as silica.Optionally, plasma gasification is split Solving melting furnace 151 can also include that reducibility gas exports, and incinerator 130 may include reducibility gas entrance, reproducibility gas Body outlet is connected to reducibility gas entrance.The reducibility gas Q6 generated in plasma gasification cracking melting furnace 151 can It is admitted in incinerator 130, using as the auxiliary fuel in garbage drying burning process.Domestic rubbish disposal is improved as a result, The energy utilization rate of system 100, realizes maximization of economic benefit.
It can be set between plasma gasification cracking melting furnace 151 and gas-solid separator 141 and incinerator 130 solid Body product collector 146.Solid resultant product collection device 146 includes the second solid waste feed inlet and the second solid waste discharge port.Wherein, second Solid waste feed inlet is connected with the first solid residue outlet of the outlet of the flying dust of gas-solid separator 141 and incinerator 130.Second is solid Useless discharge port is connected with the plasma furnace solid waste feed inlet of plasma gasification cracking melting furnace 151.That is, to burn oneself to death It burns the first solid residue of furnace 130 and the flying dust from gas-solid separator 141 enters solid via the second solid waste feed inlet first Product collector 146 then enters plasma gasification cracking melting furnace 151 from the second solid waste discharge port.By the way that solid is arranged Product collector 146 can collect the solid waste from incinerator 130 and gas-solid separator 141, to concentrate to plasma Material is put into gasification cracking melting furnace 151.
Further, the molten product obtained is admitted in molten slag discharge quenching apparatus 152 and carries out quenching, with Form the glassy particles of safety.Molten slag discharge quenching apparatus 152 is connected to slag collector 153, to collect glassy state Particle.Glassy particles can be used as construction material 160 after detecting safety and carry out secondary use.
After domestic garbage treating system 100 according to the present invention is to the processing of house refuse 110, on the one hand, the gas of generation The ingredient of emission cleans, and will not cause secondary pollution to atmosphere after discharge;On the other hand, the solid product volume of generation is more It is small, safer, it can be secondary use, be truly realized " innoxious, minimizing, recycling ".
Optionally, flue gas separation unit can also include air preheater 142.Air preheater 142 may include high temperature Smoke inlet, low-temperature flue gas outlet, the first cool air inlet and hot air outlet.Wherein, high-temperature flue gas entry and incinerator 130 High-temperature flue gas outlet be connected, low-temperature flue gas outlet is connected with the gas inlet of gas-solid separator 141.That is, air is pre- Hot device 142 can be set between incinerator 130 and gas-solid separator 141.Further, the first cool air inlet is used for sky Cold air Q2 is passed through in air preheater 142.For example, as shown in Figure 1, in the shown embodiment, cold air Q2 can pass through drum Blower 144 is blasted in air preheater 142.By the way that air preheater 142 is arranged, the height from incinerator 130 can be made Warm flue gas Q1 carries out heat with cold air Q2 and exchanges, so that the waste heat that cold air Q2 absorbs high-temperature flue gas Q1 becomes hot-air Q3, High-temperature flue gas Q1 is made to become low-temperature flue gas Q4 simultaneously.
Further, drying device 121 may include the first hot air inlet, and plasma gasification cracks melting furnace 151 Including the second hot air inlet.The hot-air of first hot air inlet and the second hot air inlet with air preheater 142 goes out Mouth connection.Specifically, a part of in the hot-air Q3 from air preheater 142 can be delivered to drying device 121, with for The dry house refuse 110 of drying device 121 provides heat;Another part can be delivered to plasma gasification cracking melting furnace 151, a small amount of air required for melting cracks is carried out to provide plasma gasification cracking melting furnace 151.Thus, it is possible to effectively Ground improves the systematic heat utilization rate of domestic garbage treating system 100, reduces operating cost.
Optionally, drying device 121 may include the second cold-air vent, and incinerator 130 may include the second cold air Entrance, the second cold-air vent are connected to the second cool air inlet.Hot-air Q3 in drying device 121 is by dry life rubbish The second cold air Q5, the second cold air Q5 is obtained after rubbish 110 to enter incinerator 130 via the second cool air inlet, at For the combustion air of incinerator 130.Thus, it is possible to which the operating cost of domestic garbage treating system 100 is effectively reduced, the energy is improved Utilization rate.
According to the another aspect of invention, a kind of life refuse processing method is additionally provided, following steps are specifically included:
House refuse 110 is sent into pretreatment unit and carries out pre-treatment step, obtains pretreating waste;
Pretreating waste feeding incinerator 130 is burned, high-temperature flue gas Q1 and the first solid residue are obtained;
High-temperature flue gas Q1 is sent into gas-solid separator 141, obtains the first exhaust gas Q7 and flying dust;
First exhaust gas Q7 is sent into flue gas purification device 143, obtains the gaseous effluent for capableing of direct emission;And
First solid residue and flying dust are sent into plasma gasification and crack melting furnace 151, molten product is obtained, will melt Product is sent into molten slag discharge quenching apparatus 152 and carries out quenching, obtains glassy particles.
When handling house refuse 110 using life refuse processing method according to the present invention, on the one hand, the gas of generation is arranged The ingredient cleaning for putting object, will not cause secondary pollution to atmosphere after discharge;On the other hand, the solid product volume of generation it is smaller, It is safer, it can be secondary use, be truly realized " innoxious, minimizing, recycling ".
Optionally, life refuse processing method according to the present invention can also include the following steps:
The feeding crusher 122 of house refuse 110 is crushed, broken house refuse is obtained;And
Broken house refuse is sent into the drying of drying device 121, obtains pretreating waste.
House refuse 110 can be broken in crusher 122 as a result, obtain the smaller broken life rubbish of multiple volumes Rubbish.Broken house refuse has bigger specific surface area compared to house refuse 110, and thereby, it is possible to increase broken house refuse Accessible area in the subsequent processing steps such as drying steps, burn down step saves the processing time of technique, improves Treatment effeciency, improves treatment effect.
In order to further increase the energy utilization rate of domestic garbage treating system 100 according to the present invention, reduce operation at This, which can also include the following steps:
High-temperature flue gas Q1 and cold air Q2 is sent into air preheater 142, so that high-temperature flue gas Q1 and cold air Q2 are in sky It exchanges heat in air preheater 142, obtains low-temperature flue gas Q4 and hot-air Q3;And
Low-temperature flue gas Q4 is sent into gas-solid separator 141, hot-air Q3 is sent into pretreatment unit and plasma gasification Crack melting furnace 151.
It, can be with that is, burn the high-temperature flue gas Q1 of generation in incinerator 130 before entering gas-solid separator 141 It is admitted to air preheater 142.In air preheater 142, energy exchange occurs for high-temperature flue gas Q1 and cold air Q2, so that high The heat transfer of warm flue gas Q1 gives cold air Q2, obtains low-temperature flue gas Q4 and hot-air Q3.Further, hot-air Q3 is in drying For drying house refuse 110 in device 121;Hot-air Q3 is solid for providing in plasma gasification cracking melting furnace 151 Body waste material reacts required a small amount of air.
Still optionally further, life refuse processing method can also include the following steps:Hot-air Q3 is in pretreatment unit In exchange heat, obtain the second cold air Q5, by the second cold air Q5 be sent into incinerator 130.That is, in drying device Heat exchange is carried out in 121, hot-air Q3, which becomes the second cold air Q5, the second cold air Q5, can be further used as incinerator Combustion air in 130.
Optionally, generating in plasma gasification cracking melting furnace 151 has reducibility gas, and reducibility gas feeding is burnt Burn furnace 130.Reducibility gas may be used as the combustion-supporting gas in incinerator 130 as a result, improve the utilization rate of the energy.
In order to further increase working efficiency, flying dust and the first solid residue can be sent into solid resultant product collection device 146, Flying dust and the first solid residue are sent into plasma gasification cracking melting furnace 151 after assembling in solid resultant product collection device 146.By This, can crack in melting furnace 151 to plasma gasification and concentrate investment material.It is alternatively possible to molten slag be discharged anxious The glassy particles being discharged in device for cooling 152 are sent into slag collector 153.As a result, glassy particles can be received by concentrating Secondary use is carried out as construction material 160 after collection.
Unless otherwise defined, technical and scientific term used herein and those skilled in the art of the invention Normally understood meaning is identical.Term used herein is intended merely to describe specifically to implement purpose, it is not intended that limitation is originally Invention.The terms such as herein presented " portion ", " part " can both indicate single part, can also indicate multiple parts Combination.The terms such as herein presented " installation ", " setting " can both indicate that a component was attached directly to another portion Part can also indicate that a component is attached to another component by middleware.It describes in one embodiment herein Feature can be applied in combination another embodiment individually or with other features, unless this feature is in another implementation It is not suitable for or is otherwise noted in mode.
The present invention has been explained by the above embodiments, but it is to be understood that, above-described embodiment is only intended to The purpose of citing and explanation, is not intended to limit the invention to the scope of the described embodiments.Furthermore those skilled in the art It is understood that the present invention is not limited to the above embodiments, introduction according to the present invention can also be made more kinds of member Variants and modifications, all fall within the scope of the claimed invention for these variants and modifications.Protection scope of the present invention by The appended claims and its equivalent scope are defined.

Claims (13)

1. a kind of domestic garbage treating system, which is characterized in that including:
Pretreatment unit, the pretreatment unit include house refuse import and pretreating waste outlet;
Incinerator, the incinerator include pretreating waste import, and high-temperature flue gas outlet and the first solid residue export, described pre- Processing garbage inlet is connected with pretreating waste outlet;
Flue gas separation unit, the flue gas separation unit include gas-solid separator, and the gas-solid separator includes gas inlet, flies Ash outlet and the first waste gas outlet, the gas inlet are connected with the high-temperature flue gas outlet;
Flue gas purification device, the flue gas purification device include that the first exhaust gas entrance and gaseous effluent export, and described first is useless Gas entrance is connected with first waste gas outlet;And
Plasma gasification cracks melting plant, and the plasma gasification cracking melting plant includes interconnected plasma Body gasification cracking melting furnace and molten slag discharge quenching apparatus, and the plasma gasification cracking melting furnace includes plasma Furnace solid waste feed inlet, the plasma furnace solid waste feed inlet and the flying dust export and first solid residue outlet connects Logical, the molten slag discharge quenching apparatus is connected to slag collector.
2. domestic garbage treating system according to claim 1, which is characterized in that the flue gas separation unit further includes sky Air preheater, the air preheater include:
High-temperature flue gas entry, the high-temperature flue gas entry are connected with the high-temperature flue gas outlet;
Low-temperature flue gas outlet, the low-temperature flue gas outlet are connected with the gas inlet;
First cool air inlet, first cool air inlet is for being passed through cold air into the air preheater;And
Hot air outlet.
3. domestic garbage treating system according to claim 1, which is characterized in that the plasma gasification cracking melting Furnace further includes reducibility gas outlet, and the incinerator includes reducibility gas entrance, reducibility gas outlet with it is described The connection of reducibility gas entrance.
4. domestic garbage treating system according to claim 2, which is characterized in that the pretreatment unit includes crusher And drying device, the crusher include the house refuse import and crush house refuse outlet, the drying device includes Crush house refuse import and pretreating waste outlet, crushings house refuse outlet and the crushing house refuse into Mouth is connected.
5. domestic garbage treating system according to claim 4, which is characterized in that the drying device includes that the first heat is empty Gas entrance, plasma gasification cracking melting furnace include the second hot air inlet, first hot air inlet and described Second hot air inlet is connected to the hot air outlet.
6. domestic garbage treating system according to claim 4, which is characterized in that the drying device further includes second cold Air outlet slit, the incinerator include the second cool air inlet, second cold-air vent and second cool air inlet Connection.
7. domestic garbage treating system according to claim 1, which is characterized in that the plasma gasification cracking melting Solid resultant product collection device is set between furnace and the gas-solid separator and the incinerator, and the solid resultant product collection device includes Second solid waste feed inlet and the second solid waste discharge port, the second solid waste feed inlet and the flying dust export and described first consolidates Body solid discharge is connected, and the second solid waste discharge port is connected with the plasma furnace solid waste feed inlet.
8. a kind of life refuse processing method, which is characterized in that include the following steps:
House refuse is sent into pretreatment unit and carries out pre-treatment step, obtains pretreating waste;
The pretreating waste is sent into incinerator to burn, obtains high-temperature flue gas and the first solid residue;
The high-temperature flue gas is sent into gas-solid separator, obtains the first exhaust gas and flying dust;
First exhaust gas is sent into flue gas purification device, obtains the gaseous effluent for capableing of direct emission;And
First solid residue and the flying dust are sent into plasma gasification and crack melting furnace, molten product is obtained, by institute It states molten product and is sent into molten slag discharge quenching apparatus progress quenching, obtain glassy particles.
9. life refuse processing method according to claim 8, which is characterized in that the life refuse processing method also wraps Include following steps:
The high-temperature flue gas and cold air are sent into air preheater, so that the high-temperature flue gas and the cold air are in the sky It exchanges heat in air preheater, obtains low-temperature flue gas and hot-air;And
The low-temperature flue gas is sent into the gas-solid separator, by the hot-air be sent into the pretreatment unit and it is described etc. from Daughter gasification cracking melting furnace.
10. life refuse processing method according to claim 9, which is characterized in that the life refuse processing method is also Include the following steps:
The hot-air exchanges heat in the pretreatment unit, obtains the second cold air, and second cold air is sent into The incinerator.
11. life refuse processing method according to claim 8, which is characterized in that consolidate the flying dust and described first Body residue is sent into solid resultant product collection device, and the flying dust and first solid residue are assembled in the solid resultant product collection device After be sent into plasma gasification cracking melting furnace.
12. life refuse processing method according to claim 8, which is characterized in that the plasma gasification cracking is molten Melt to generate in furnace and have reducibility gas, the reducibility gas is sent into the incinerator.
13. life refuse processing method according to claim 8, which is characterized in that the pre-treatment step includes:
The house refuse is sent into broken crusher machine, obtains broken house refuse;And
The broken house refuse is sent into drying device drying, obtains pretreating waste.
CN201810763719.9A 2018-07-12 2018-07-12 Domestic garbage treating system and life refuse processing method Pending CN108826318A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810763719.9A CN108826318A (en) 2018-07-12 2018-07-12 Domestic garbage treating system and life refuse processing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810763719.9A CN108826318A (en) 2018-07-12 2018-07-12 Domestic garbage treating system and life refuse processing method

Publications (1)

Publication Number Publication Date
CN108826318A true CN108826318A (en) 2018-11-16

Family

ID=64136155

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810763719.9A Pending CN108826318A (en) 2018-07-12 2018-07-12 Domestic garbage treating system and life refuse processing method

Country Status (1)

Country Link
CN (1) CN108826318A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110404926A (en) * 2019-07-05 2019-11-05 上海齐耀热能工程有限公司 A kind of corona treatment organic waste system
CN110513703A (en) * 2019-09-06 2019-11-29 西安交通大学 A kind of waste incineration and fusing fly ash solidify federated resource processing system
CN110695055A (en) * 2019-10-20 2020-01-17 安徽航天环境工程有限公司 Red mud cracking treatment method
CN110695057A (en) * 2019-10-20 2020-01-17 安徽航天环境工程有限公司 Oil sludge cracking treatment method
CN110715297A (en) * 2019-10-15 2020-01-21 武汉丰盈能源技术工程有限公司 Harmless treatment system and method for plasma gasification furnace and waste incineration power plant
CN112923353A (en) * 2021-01-13 2021-06-08 西安交通大学 Gasification fly ash utilization system and method
CN113897077A (en) * 2021-11-16 2022-01-07 航天环境工程有限公司 Continuous purification device of pyrolysis carbon black high temperature plasma

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104976622A (en) * 2015-08-05 2015-10-14 中国东方电气集团有限公司 Household garbage classified gasification system with rotary kiln gasification and plasma fusion capability
CN106642159A (en) * 2017-02-27 2017-05-10 西安航天源动力工程有限公司 Recycling hazardous waste treatment system and treatment method by synergizing rotary kiln and plasma gasification
CN206531067U (en) * 2016-12-12 2017-09-29 神雾科技集团股份有限公司 A kind of system of refuse pyrolysis gasification and melting
CN208536005U (en) * 2018-07-12 2019-02-22 上海齐耀热能工程有限公司 Domestic garbage treating system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104976622A (en) * 2015-08-05 2015-10-14 中国东方电气集团有限公司 Household garbage classified gasification system with rotary kiln gasification and plasma fusion capability
CN206531067U (en) * 2016-12-12 2017-09-29 神雾科技集团股份有限公司 A kind of system of refuse pyrolysis gasification and melting
CN106642159A (en) * 2017-02-27 2017-05-10 西安航天源动力工程有限公司 Recycling hazardous waste treatment system and treatment method by synergizing rotary kiln and plasma gasification
CN208536005U (en) * 2018-07-12 2019-02-22 上海齐耀热能工程有限公司 Domestic garbage treating system

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110404926A (en) * 2019-07-05 2019-11-05 上海齐耀热能工程有限公司 A kind of corona treatment organic waste system
CN110404926B (en) * 2019-07-05 2024-04-12 上海齐耀热能工程有限公司 System for treating organic waste by plasma
CN110513703A (en) * 2019-09-06 2019-11-29 西安交通大学 A kind of waste incineration and fusing fly ash solidify federated resource processing system
CN110715297A (en) * 2019-10-15 2020-01-21 武汉丰盈能源技术工程有限公司 Harmless treatment system and method for plasma gasification furnace and waste incineration power plant
CN110695055A (en) * 2019-10-20 2020-01-17 安徽航天环境工程有限公司 Red mud cracking treatment method
CN110695057A (en) * 2019-10-20 2020-01-17 安徽航天环境工程有限公司 Oil sludge cracking treatment method
CN110695057B (en) * 2019-10-20 2021-07-27 航天神禾(北京)环保有限公司 Oil sludge cracking treatment method
CN110695055B (en) * 2019-10-20 2021-08-13 航天神禾(北京)环保有限公司 Red mud cracking treatment method
CN112923353A (en) * 2021-01-13 2021-06-08 西安交通大学 Gasification fly ash utilization system and method
CN113897077A (en) * 2021-11-16 2022-01-07 航天环境工程有限公司 Continuous purification device of pyrolysis carbon black high temperature plasma

Similar Documents

Publication Publication Date Title
CN108826318A (en) Domestic garbage treating system and life refuse processing method
WO2019095964A1 (en) Treatment method and device for cooperatively burning garbage and semi-dry sludge
CN102513346B (en) Thermal desorption method and device for organic polluted soil on basis of cement process
CN208536005U (en) Domestic garbage treating system
CN104438296A (en) Dry-process rotary cement kiln cooperative household garbage treatment system and treatment method
CN106642159A (en) Recycling hazardous waste treatment system and treatment method by synergizing rotary kiln and plasma gasification
CN105864782A (en) Device and method for heating and melting rubbish under oxygen-rich condition
CN108194926A (en) A kind of dangerous waste incineration processing method and its system
CN101476729A (en) Drying pretreatment method and device for urban domestic garbage
CN105945028B (en) Consumer waste incineration regeneration technique
CN204276506U (en) A kind of dry method cement rotary kiln associated treatment house refuse system
CN206701931U (en) A kind of building waste processing system
CN207514918U (en) A kind of rubbish cooperates with incinerating and treating device with semi-dry sludge
CN107606623B (en) Small garbage gas-carbon complementary carbonization combustion furnace
CN102344259A (en) Environmental-protection and energy-saving garbage incineration and waste gas utilization device
CN109323263A (en) A kind of environmental protecting device with waste incineration classification processing conveying function
CN106881336A (en) Refuse disposal system
CN105222136A (en) A kind of system of cement kiln cooperative disposal house refuse
CN207162549U (en) A kind of refuse pyrolysis gasification combustion furnace
CN105275517A (en) Cement kiln waste heat power generation system utilizing waste incineration flue gas
CN210718694U (en) Hazardous waste workshop waste gas cooperative disposal system
CN211345325U (en) System for organic solid waste incineration melting innocent treatment
CN211694905U (en) Automatic change industrial waste incineration and resource recovery processing apparatus
CN207661783U (en) A kind of small-sized rubbish gas charcoal complementation charing combustion furnace
KR200178486Y1 (en) Drying melting process for waste and sludge

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination