CN213746770U - Biomass comprehensive organic waste treatment heat supply device - Google Patents
Biomass comprehensive organic waste treatment heat supply device Download PDFInfo
- Publication number
- CN213746770U CN213746770U CN202022676636.1U CN202022676636U CN213746770U CN 213746770 U CN213746770 U CN 213746770U CN 202022676636 U CN202022676636 U CN 202022676636U CN 213746770 U CN213746770 U CN 213746770U
- Authority
- CN
- China
- Prior art keywords
- biomass
- exhaust
- flue gas
- heat boiler
- organic solid
- 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.)
- Active
Links
Images
Landscapes
- Gasification And Melting Of Waste (AREA)
Abstract
The utility model discloses an organic waste treatment heating device is synthesized to living beings, including combustion system, exhaust-heat boiler system and flue gas purification system, combustion system divide into to accompany to burn the structure, burn the structure after and the pyrolysis burns the structure, exhaust-heat boiler system includes exhaust-heat boiler, boiler dust exhaust equipment is installed to the exhaust-heat boiler below, the last economizer that installs of exhaust-heat boiler, the economizer has the softened water tank through the feed pump intercommunication, flue gas purification system includes sack dust fall ware, dust fall ware dust exhaust equipment is installed to sack dust fall ware below, the exhaust port intercommunication of sack dust fall ware has the draught fan, combustion system's flue gas passageway and exhaust-heat boiler system are linked together. A biomass integrated organic waste treatment heating device, adopt living beings companion to burn, after burn, the pyrolysis is burnt the mode and is handled organic solid useless, outside heat supply realizes organic harmless, the utilization useless resource admittedly.
Description
Technical Field
The utility model relates to a living beings organic waste treatment technical field especially relates to a living beings are synthesized organic waste and are handled heating device.
Background
In view of the enhancement of environmental awareness, the execution of environmental policy, the harmless treatment of organic solid wastes, and the resource utilization are also a major subject direction; the conventional traditional consciousness of environment-friendly enterprises is that large-scale enterprises are made to be strong, so that large-scale roads are always concentrated on the scale design of organic solid waste treatment, and due to the overlarge coverage area and the idealized data design and analysis, the current situations of insufficient eating, high cost, low profit and difficult operation appear in organic solid waste operation; the main factors are large-scale design, the total amount of the organic solid wastes is insufficient, the coverage area is large, the solid waste transportation cost is high, the profit is reduced, and partial resources in the production process cannot be reused and the utilization rate is low due to centralized treatment, so the current situation that the organic solid waste treatment enterprises are difficult to operate appears; the biomass comprehensive organic solid waste treatment heat supply device is a distributed utilization way, and biomass is treated and converted into heat energy for supply by using combustion modes such as biomass co-combustion, after-combustion, pyrolysis combustion and the like, so that harmless and resource utilization of organic solid waste is realized.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a biomass synthesis organic waste handles heating device, mainly used living beings accompany burns, after burns, the pyrolysis burns organic solid useless outside heat supply, realizes organic harmless, the resource utilization useless admittedly.
In order to achieve the above purpose, the utility model provides a technical scheme is: including combustion system, exhaust-heat boiler system and flue gas purification system, combustion system divide into to accompany to burn the structure, after burn the structure and the pyrolysis burns the structure, exhaust-heat boiler system includes exhaust-heat boiler, the boiler ash discharge equipment is installed to the exhaust-heat boiler below, the last economizer that installs of exhaust-heat boiler, the economizer has the softened water tank through boiler feed pump intercommunication, flue gas purification system includes sack dust fall ware, dust fall ware ash discharge equipment is installed to sack dust fall ware below, the exhaust port intercommunication of sack dust fall ware has the draught fan, combustion system's flue gas passageway and exhaust-heat boiler system are linked together, exhaust-heat boiler system's flue gas passageway and flue gas purification system want the intercommunication.
Further, the combustion accompanying structure comprises a first biomass combustion furnace, the first biomass combustion furnace is communicated with a stirring device through a feeding device, a first slag discharging device is installed at the bottom of a hearth of the first biomass combustion furnace, the first biomass combustion furnace is communicated with a first air feeder, and a flue gas channel of the first biomass combustion furnace is communicated with a waste heat boiler.
Further, the post-sintering mechanism comprises a second biomass combustion furnace and an organic solid waste combustion furnace, wherein the second biomass combustion furnace is communicated with a biomass feeding device, a second slag discharge device is arranged below the second biomass combustion furnace, the second biomass combustion furnace is communicated with a second air feeder, a third slag discharge device is arranged on the organic solid waste combustion furnace, the organic solid waste combustion furnace is communicated with a third air feeder, a water cooling wall is fixed on the outer wall of the organic solid waste combustion furnace, and a flue gas channel of the organic solid waste combustion furnace and a flue gas channel of the second biomass combustion furnace are communicated with the waste heat boiler.
Further, the pyrolysis sintering mechanism comprises an organic solid waste pyrolysis furnace, a biomass combustion chamber and an organic solid waste pyrolysis gas secondary combustion chamber are arranged in the organic solid waste pyrolysis furnace, fourth slag discharge equipment is respectively arranged on the organic solid waste pyrolysis furnace and the biomass combustion chamber, a fourth air feeder is respectively communicated with the organic solid waste pyrolysis furnace and the biomass combustion chamber, and a flue gas channel of the organic solid waste pyrolysis furnace is communicated with the waste heat boiler.
Further, a co-combustion structure process of the biomass comprehensive organic waste treatment heat supply device comprises the following steps:
1) the biomass fuel and the solid organic solid waste are fed into a stirring device for stirring, the mixture is fed into a first biomass combustion furnace through a feeding device after being stirred, the liquid organic solid waste is sprayed into the first biomass combustion furnace for combustion, and a first air feeder is started to feed air to the first biomass combustion furnace for full combustion;
2) treating waste heat of the boiler, wherein the flue gas in the step 1) enters a waste heat boiler through a flue gas channel of a first biomass combustion furnace to heat boiler water, the waste heat boiler conveys steam to a pipeline, a boiler water-feeding pump injects water in a soft water tank into the boiler through an economizer, and when the ash in an ash hopper of the waste heat boiler is excessive, boiler ash discharging equipment is started to discharge the water;
3) flue gas purification, the flue gas of step 2) passes through exhaust-heat boiler's flue gas passageway and gets into sack dust fall ware and carry out the dust fall and handle, and the dust after the processing is discharged through dust fall ware ash discharge equipment, opens the draught fan, discharges the flue gas from the chimney, and when the interior smoke and dust of sack dust fall ware was too much, opened dust fall ware ash discharge equipment and discharged cigarette ash.
Further, the post-sintering structure process of the biomass comprehensive organic waste treatment heat supply device comprises the following steps:
1) and (3) combustion, namely sending the liquid organic solid waste and the solid organic solid waste into an organic solid waste incinerator for combustion, starting a third air feeder for air supply and auxiliary combustion, sending the biomass fuel into a second biomass combustion furnace through biomass feeding equipment, and starting a second air feeder for air supply and auxiliary combustion.
2) Treating waste heat of the boiler, wherein the flue gas in the step 1) enters a waste heat boiler through a flue gas channel of the organic solid waste incinerator and a flue gas channel of a second biomass combustion furnace to heat boiler water, the waste heat boiler conveys steam to a pipeline, a boiler water supply system injects water in a soft water tank into the boiler through an economizer, and when the ash in an ash bucket of the waste heat boiler is excessive, boiler ash discharge equipment is started to discharge the excessive ash;
3) flue gas purification, the flue gas of step 2) passes through exhaust-heat boiler's flue gas passageway and gets into sack dust fall ware and carry out the dust fall and handle, and the dust after the processing is discharged through dust fall ware ash discharge equipment, opens the draught fan, discharges the flue gas from the chimney, and when the interior smoke and dust of sack dust fall ware was too much, opened dust fall ware ash discharge equipment and discharged cigarette ash.
Further, a pyrolysis sintering structure process of the biomass comprehensive organic waste treatment heat supply device comprises the following steps:
1) the method comprises the following steps of (1) combustion, namely feeding liquid organic solid waste and solid organic solid waste into an organic solid waste pyrolysis furnace for pyrolysis, spraying biomass fuel into a biomass combustion chamber for combustion, starting a fourth air blower for air supply and auxiliary combustion, feeding the mixed flue gas after combustion into an organic solid waste pyrolysis gas secondary combustion chamber for secondary combustion, starting another fourth air blower for air supply and auxiliary combustion;
2) treating waste heat of the boiler, wherein the flue gas in the step 1) enters a waste heat boiler through a flue gas channel of an organic solid waste pyrolysis gas secondary combustion chamber to heat boiler water, the waste heat boiler conveys steam to a pipeline, a boiler water supply system injects water in a soft water tank into the boiler through an economizer, and when the ash in an ash bucket of the waste heat boiler is excessive, boiler ash discharge equipment is started to discharge the water;
3) flue gas purification, the flue gas of step 2) passes through exhaust-heat boiler's flue gas passageway and gets into sack dust fall ware and carry out the dust fall and handle, and the dust after the processing is discharged through dust fall ware ash discharge equipment, opens the draught fan, discharges the flue gas from the chimney, and when the interior smoke and dust of sack dust fall ware was too much, opened dust fall ware ash discharge equipment and discharged cigarette ash.
According to the physical characteristics of organic solid wastes, the combustion modes are divided into three combustion modes of combustion tracing, after combustion and pyrolysis combustion; the high-temperature flue gas after burning is heated by steam generated by a waste heat boiler, and the flue gas is treated by purifying equipment to reach the emission standard. The characteristics of the organic solid waste are mainly divided into two parameters of containing no heavy metal and chlorine and combustion heat value to determine the combustion mode.
A burning accompanying mode: if the organic solid waste does not contain heavy metal chlorine element and has lower heat value, adopting a direct combustion mode of combustion tracing, and realizing harmless and resource utilization of the organic solid waste by using biomass combustion tracing, wherein the combustion tracing mode refers to the mixed combustion of the organic solid waste and biomass, and is stable in heat energy output; the high-temperature flue gas after the co-combustion is subjected to heat exchange to output steam for external supply, the flue gas after heat release enters a cloth bag for dust removal, purification and emission, and the co-combustion furnace slag can be used for soil improvement.
Post-firing mode: the organic solid waste containing no heavy metal chlorine and having a higher heat value adopts a post-combustion mode, and because the biological combustion has a certain fly ash amount, and the temperature of the flue gas generated by the combustion of the organic solid waste with the high heat value is higher than the ash melting point of the fly ash, a slag layer is easily formed on a heat exchange tube of a waste heat boiler to influence heat exchange, so that the post-combustion mode is adopted, the biomass is used as a supplementary heat source, and the harmless and resource utilization of the organic solid waste is realized; the post-combustion mode adopts a double-hearth structure, high-heat-value organic solid waste is combusted in a first hearth, the first hearth is provided with a water-cooled wall, high-temperature flue gas transfers part of heat to the water-cooled wall through radiation, the temperature of the cooled flue gas is equivalent to that of biomass combustion flue gas, and the cooled flue gas enters a waste heat boiler through a flue of a second hearth; the biomass is combusted in the second hearth, the biomass is used as afterburning to adjust heat supply load, the smoke of the first and second hearths is supplied by steam output by the waste heat boiler, the discharged smoke enters the cloth bag for dust removal and purification and is discharged, the residue of the first hearth is used as a building auxiliary material, and the slag of the second hearth can be used for soil improvement.
A pyrolysis burning mode: if the organic solid waste contains heavy metals and chlorine elements, a pyrolysis combustion mode is adopted, namely biomass is combusted to serve as a pyrolysis heat source of the organic solid waste, organic solid waste pyrolysis gas is combusted, biomass flue gas is supplemented, the heavy metals and the chlorine elements are enriched in pyrolysis slag and recycled through other processes, the organic solid waste is harmless and recycled, the pyrolysis combustion is divided into two combustion structures, the main load of a biomass combustion chamber is an organic solid waste pyrolysis furnace, pyrolysis gas after the organic solid waste is pyrolyzed is combusted through secondary air distribution, high-temperature flue gas after the combustion is mixed with the biomass flue gas to enter a secondary waste heat boiler after passing through a primary heat exchanger, the biomass combustion adjusts the entering amount according to the load amount, and the pyrolysis gas amount and the biomass flue gas amount are controlled; the flue gas is output by a waste heat boiler and is externally supplied with steam, the flue gas enters a cloth bag for dust reduction, purification and emission, and the pyrolysis furnace slag can be used as a heavy metal recovery raw material.
The utility model has the advantages that: a biomass comprehensive organic waste treatment heat supply device adopts biomass co-combustion, post-combustion and pyrolysis combustion modes to treat organic solid waste and supply heat to the outside, so that harmless and resource utilization of the organic solid waste is realized.
Drawings
Fig. 1 is a schematic structural view of embodiment 1 of the present invention;
fig. 2 is a process diagram of example 1 of the present invention;
fig. 3 is a schematic structural view of embodiment 2 of the present invention;
fig. 4 is a process diagram of example 2 of the present invention;
fig. 5 is a schematic structural view of embodiment 3 of the present invention;
fig. 6 is a process diagram of example 3 of the present invention.
Detailed Description
Example 1
As shown in fig. 1-2, organic waste treatment heating device is synthesized to living beings, including combustion system, exhaust-heat boiler system and gas cleaning system, combustion system divide into to accompany to burn the structure, burn the structure after with the pyrolysis and burn the structure, exhaust-heat boiler system includes exhaust-heat boiler 1, boiler dust discharging equipment 2 is installed to exhaust-heat boiler 1 below, install economizer 3 on the exhaust-heat boiler 1, economizer 3 has soft water tank 5 through boiler feed pump 4 intercommunication, gas cleaning system includes sack dust fall ware 6, dust fall ware dust discharging equipment 7 is installed to sack dust fall ware 6 below, the exhaust port intercommunication of sack dust fall ware 6 has draught fan 8, combustion system's flue gas passageway and exhaust-heat boiler system are linked together, exhaust-heat boiler system's flue gas passageway and gas cleaning system want the intercommunication.
The combustion accompanying structure comprises a first biomass combustion furnace 11, wherein the first biomass combustion furnace 11 is communicated with a stirring device 13 through a feeding device 12, a first slag discharging device 14 is installed at the bottom of a hearth of the first biomass combustion furnace 11, the first biomass combustion furnace 11 is communicated with a first air blower 15, and a flue gas channel of the first biomass combustion furnace 11 is communicated with the waste heat boiler 1.
A co-combustion structure process of a biomass comprehensive organic waste treatment heat supply device comprises the following steps:
1) the biomass fuel and the solid organic solid waste are sent into a stirring device 13 to be stirred, the biomass fuel and the solid organic solid waste are sent into a first biomass combustion furnace 11 through a feeding device 12 after being stirred, the liquid organic solid waste is sprayed into the first biomass combustion furnace 11 to be combusted, and a first air blower 15 is started to supply air to the first biomass combustion furnace 11 for full combustion;
2) treating the waste heat of the boiler, wherein the flue gas in the step 1) enters a waste heat boiler 1 through a flue gas channel of a first biomass combustion furnace 11 to heat boiler water, the waste heat boiler 1 conveys steam to a pipeline, a boiler water feeding pump 4 injects water in a soft water tank 5 into the boiler through an economizer 3, and when the ash in an ash hopper of the waste heat boiler 1 is excessive, a boiler ash discharging device 2 is started to discharge the ash;
3) flue gas purification, the flue gas of step 2) passes through exhaust-heat boiler 1's flue gas passageway and gets into sack dust fall ware 6 and carries out the dust fall and handle, and the dust after the processing is discharged through dust fall ware ash discharge equipment 7, opens draught fan 8, discharges the flue gas from the chimney, and when the smoke and dust was too much in sack dust fall ware 6, it discharges ash equipment 7 discharge cigarette ashes to open the dust fall ware.
Example 2
Based on embodiment 1, as shown in fig. 3 to 4, the post-sintering mechanism includes a second biomass combustion furnace 21 and an organic solid waste incinerator 24, the second biomass combustion furnace 21 is communicated with a biomass feeding device 22, a second slag discharging device 221 is installed below the second biomass combustion furnace 21, the second biomass combustion furnace 21 is communicated with a second air blower 231, the organic solid waste incinerator 24 is installed with a third slag discharging device 222, the organic solid waste incinerator 24 is communicated with a third air blower 232, a water cooling wall 25 is fixed on an outer wall of the organic solid waste incinerator 24, and a flue gas passage of the organic solid waste incinerator 24 and a flue gas passage of the second biomass combustion furnace 21 are communicated with the waste heat boiler 1.
A post-sintering structure process of a biomass comprehensive organic waste treatment heat supply device comprises the following steps:
1) and (3) combustion, namely sending the liquid organic solid waste and the solid organic solid waste into the organic solid waste incinerator 24 for combustion, starting the third air blower 232 to blow air for auxiliary combustion, sending the biomass fuel into the second biomass combustion furnace 21 through the biomass feeding equipment 22, spraying the liquid organic solid waste into the second biomass combustion furnace 21 for combustion, and starting the second air blower 231 to blow air for auxiliary combustion.
2) Treating the waste heat of the boiler, wherein the flue gas in the step 1) enters a waste heat boiler 1 through a flue gas channel of an organic solid waste incinerator 24 and a flue gas channel of a second biomass combustion furnace 21 to heat boiler water, the waste heat boiler 1 conveys steam to a pipeline, a boiler water feed pump 4 injects the water in a soft water tank 5 into the boiler through an economizer 3, and when the ash in an ash hopper of the waste heat boiler 1 is excessive, a boiler ash discharge device 2 is started to discharge the ash;
3) flue gas purification, the flue gas of step 2) passes through exhaust-heat boiler 1's flue gas passageway and gets into sack dust fall ware 6 and carries out the dust fall and handle, and the dust after the processing is discharged through dust fall ware ash discharge equipment 7, opens draught fan 8, discharges the flue gas from the chimney, and when the smoke and dust was too much in sack dust fall ware 6, it discharges ash equipment 7 discharge cigarette ashes to open the dust fall ware.
Example 3
Based on embodiment 1, as shown in fig. 5 to 6, the pyrolysis sintering mechanism includes an organic solid waste pyrolysis furnace 31, a biomass combustion chamber 32 and an organic solid waste pyrolysis gas second combustion chamber 33 are disposed in the organic solid waste pyrolysis furnace 31, fourth slag discharge devices 34 are respectively disposed on the organic solid waste pyrolysis furnace 31 and the biomass combustion chamber 32, fourth blowers 35 are respectively communicated with the organic solid waste pyrolysis furnace 31 and the biomass combustion chamber 32, and a flue gas channel of the organic solid waste pyrolysis furnace 31 is communicated with the waste heat boiler 1.
A pyrolysis sintering structure process of a biomass comprehensive organic waste treatment heat supply device comprises the following steps:
1) burning, namely sending liquid organic solid waste and solid organic solid waste into an organic solid waste pyrolysis furnace 31 for pyrolysis, spraying biomass fuel into a biomass combustion chamber 32 for combustion, starting a fourth air blower 35 for air supply and auxiliary combustion, enabling the burned mixed flue gas to enter an organic solid waste pyrolysis gas secondary combustion chamber 33 for secondary combustion, starting another fourth air blower 35 for air supply and auxiliary combustion;
2) treating the waste heat of the boiler, wherein the flue gas in the step 1) enters a waste heat boiler 1 through a flue gas channel of an organic solid waste pyrolysis gas secondary combustion chamber 33 to heat boiler water, the waste heat boiler 1 conveys steam to a pipeline, a boiler water feed pump 4 injects water in a soft water tank 5 into the boiler through an economizer 3, and when the ash in an ash hopper of the waste heat boiler 1 is excessive, a boiler ash discharge device 2 is started to discharge the ash;
3) flue gas purification, the flue gas of step 2) passes through exhaust-heat boiler 1's flue gas passageway and gets into sack dust fall ware 6 and carries out the dust fall and handle, and the dust after the processing is discharged through dust fall ware ash discharge equipment 7, opens draught fan 8, discharges the flue gas from the chimney, and when the smoke and dust was too much in sack dust fall ware 6, it discharges ash equipment 7 discharge cigarette ashes to open the dust fall ware.
According to the biomass comprehensive organic waste treatment and heat supply device, organic solid waste is treated in biomass co-firing, post-firing and pyrolysis firing modes, heat is supplied to the outside, and harmless and resource utilization of the organic solid waste is realized.
Claims (4)
1. The utility model provides a biomass integrated organic waste handles heating device which characterized in that: including combustion system, exhaust-heat boiler system and flue gas purification system, combustion system divide into to accompany to burn the structure, after burn the structure and the pyrolysis burns the structure, exhaust-heat boiler system includes exhaust-heat boiler (1), boiler dust discharging equipment (2) is installed to exhaust-heat boiler (1) below, install economizer (3) on exhaust-heat boiler (1), economizer (3) have soft water tank (5) through boiler feed pump (4) intercommunication, flue gas purification system includes sack dust fall ware (6), dust fall ware dust discharging equipment (7) is installed to sack dust fall ware (6) below, the exhaust port intercommunication of sack dust fall ware (6) has draught fan (8), combustion system's flue gas passageway and exhaust-heat boiler system are linked together, exhaust-heat boiler system's flue gas passageway and flue gas purification system want the intercommunication.
2. The heat supply apparatus for comprehensive organic waste treatment of biomass according to claim 1, wherein: the combustion accompanying structure comprises a first biomass combustion furnace (11), wherein the first biomass combustion furnace (11) is communicated with a stirring device (13) through a feeding device (12), a first slag discharging device (14) is installed at the bottom of a hearth of the first biomass combustion furnace (11), the first biomass combustion furnace (11) is communicated with a first air feeder (15), and a flue gas channel of the first biomass combustion furnace (11) is communicated with a waste heat boiler (1).
3. The heat supply apparatus for comprehensive organic waste treatment of biomass according to claim 1, wherein: the post-sintering mechanism comprises a second biomass combustion furnace (21) and an organic solid waste incinerator (24), wherein the second biomass combustion furnace (21) is communicated with a biomass feeding device (22), a second slag discharging device (221) is installed below the second biomass combustion furnace (21), the second biomass combustion furnace (21) is communicated with a second air blower (231), a third slag discharging device (222) is installed on the organic solid waste incinerator (24), the organic solid waste incinerator (24) is communicated with a third air blower (232), a water cooling wall (25) is fixed on the outer wall of the organic solid waste incinerator (24), and flue gas channels of the organic solid waste incinerator (24) and the second biomass combustion furnace (21) are communicated with the waste heat boiler (1).
4. The heat supply apparatus for comprehensive organic waste treatment of biomass according to claim 1, wherein: the pyrolysis sintering structure comprises an organic solid waste pyrolysis furnace (31), a biomass combustion chamber (32) and an organic solid waste pyrolysis gas secondary combustion chamber (33) are arranged in the organic solid waste pyrolysis furnace (31), fourth slag discharge equipment (34) is respectively arranged on the organic solid waste pyrolysis furnace (31) and the biomass combustion chamber (32), a fourth air feeder (35) is respectively communicated on the organic solid waste pyrolysis furnace (31) and the biomass combustion chamber (32), and a flue gas channel of the organic solid waste pyrolysis furnace (31) is communicated with the waste heat boiler (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022676636.1U CN213746770U (en) | 2020-11-18 | 2020-11-18 | Biomass comprehensive organic waste treatment heat supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022676636.1U CN213746770U (en) | 2020-11-18 | 2020-11-18 | Biomass comprehensive organic waste treatment heat supply device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213746770U true CN213746770U (en) | 2021-07-20 |
Family
ID=76826579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022676636.1U Active CN213746770U (en) | 2020-11-18 | 2020-11-18 | Biomass comprehensive organic waste treatment heat supply device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213746770U (en) |
-
2020
- 2020-11-18 CN CN202022676636.1U patent/CN213746770U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107255285B (en) | A kind of method and system of three drivings grate furnace mixed burning house refuse and sludge | |
| CN206094112U (en) | Sludge incineration system | |
| CN203628668U (en) | Counter heating refuse incinerator | |
| CN102705837A (en) | System and method for collaborative garbage disposal of cement clinker production line | |
| CN105864782A (en) | Device and method for heating and melting rubbish under oxygen-rich condition | |
| CN207599723U (en) | Waste treatment equipment | |
| CN1430016A (en) | Slag incinerator for treating hazardous wastes and medical garbage and process method | |
| CN100432532C (en) | Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator | |
| CN103742918A (en) | Waste incineration treatment process | |
| CN105385465A (en) | Garbage pyrolyzation device and method | |
| CN102878569B (en) | High-temperature air combustion intensifying device and method applicable to low heating value mixed garbage | |
| CN102705832B (en) | Solid waste incinerator without emission of flue gas | |
| CN206055638U (en) | For the cracking incinerator of waste process of endangering | |
| CN213746770U (en) | Biomass comprehensive organic waste treatment heat supply device | |
| CN107687639A (en) | Energy-saving waste combustion waste-heat recovery device | |
| JP2001342476A (en) | Method and facility for producing carbonized waste | |
| CN110542094A (en) | Chain furnace type fly ash pre-burning melting device | |
| CN112432184A (en) | Biomass comprehensive organic waste treatment heat supply device and process thereof | |
| CN210069852U (en) | Thermal decomposition grate furnace system | |
| CN210320063U (en) | Carbonization incinerator for treating solid waste material | |
| CN210485746U (en) | Waste incinerator and waste heat recovery system thereof | |
| CN113446608A (en) | Dry cement preheating decomposition system | |
| CN102563668A (en) | Sludge and domestic garbage mixed firing grate boiler | |
| CN106568087A (en) | Garbage treatment system | |
| JP2017176970A (en) | Incineration ash treatment system and incineration ash treatment method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |