CN214937226U - System for handle organic solid useless - Google Patents
System for handle organic solid useless Download PDFInfo
- Publication number
- CN214937226U CN214937226U CN202022858390.XU CN202022858390U CN214937226U CN 214937226 U CN214937226 U CN 214937226U CN 202022858390 U CN202022858390 U CN 202022858390U CN 214937226 U CN214937226 U CN 214937226U
- Authority
- CN
- China
- Prior art keywords
- cracking
- pyrolysis
- pyrolysis gas
- organic solid
- solid waste
- 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 a system for treating organic solid waste, which comprises a cracking system, a heat supply system, a cracking gas purification system and a flue gas treatment system; the cracking system comprises an oxygen-free cracking device and a multi-stage spiral cracking unit, wherein the multi-stage spiral cracking unit is provided with a sealing device and is at least a two-stage spiral cracking device; the heating system comprises a dust remover, a burnout chamber and a heating device. The system adopts an anaerobic cracking technology, so that pollutants of dioxin cannot be generated in the cracking process, and the cracked product is mainly micromolecular cracking gas, so that the system is more environment-friendly to use; the pyrolysis gas of the organic solid waste raw material is used as a heating working medium, and the pyrolysis gas is recycled by the heating device, so that the heat exchange efficiency is increased, and the pyrolysis efficiency is improved.
Description
Technical Field
The utility model relates to a solid waste handles technical field, concretely relates to system for handle organic solid useless.
Background
The organic solid waste refers to solid and semi-solid organic waste which pollutes the environment and is generated in production, construction, production and living and other activities of human beings. Generally, the content of organic solid waste organic matters accounts for more than 20%. Nowadays, about 62 hundred million tons of organic solid wastes are produced in China every year, mainly from planting industry, animal husbandry, industrial wastes, kitchen wastes and municipal domestic wastes, and account for about 60 percent of the total solid wastes produced. On one hand, the organic solid wastes have the characteristics of more sources, large yield, complex components, unfixed composition yield and large regional difference, and the putrefactive decomposition causes great pollution to the environment; on the other hand, the organic solid waste has high organic content and is flammable and can be recycled as energy. Therefore, the method has very important practical significance for reducing, harmlessly and recycling the organic solid waste.
The main treatment modes of the organic solid wastes are landfill and incineration. However, solid waste landfill occupies a large land area, part of waste is difficult to naturally degrade, and the waste exists for a long time in the landfill process, and causes secondary pollution to soil and water; the organic solid waste has obvious effect of reducing quantity by burning, and can recover partial heat energy, but the burning can cause serious environmental pollution, and harmful substances such as dioxin, acid gas, fly ash and the like are generated, and meanwhile, the related equipment is damaged. Along with the acceleration of the urbanization process, the structure of the solid waste is changed while the solid waste is increased: the organic matters are increased, the combustible matters are increased, and the available value is increased.
SUMMERY OF THE UTILITY MODEL
In order to overcome the defects of the prior art, the utility model aims to provide a system for treating organic solid waste, which adopts an anaerobic cracking technology to treat organic solid waste, so that the system is converted into cracking gas, and pollutants such as dioxin can not be generated in the cracking process. Pyrolysis gas gets back to anaerobic cracking device again after the heating and uses, improves heat exchange efficiency, promotes the cracking efficiency.
The purpose of the utility model is realized by adopting the following technical scheme:
a system for treating organic solid waste comprises a cracking system, a heat supply system, a cracking gas purification system and a flue gas treatment system; the cracking system comprises an oxygen-free cracking device and a multi-stage spiral cracking unit, wherein the multi-stage spiral cracking unit is provided with a sealing device and comprises at least two stages of spiral cracking devices; the heating system comprises a dust remover, a burnout chamber and a heating device;
a pyrolysis gas outlet of the anaerobic pyrolysis device is connected with a pyrolysis gas inlet of the dust remover; the pyrolysis gas outlet of the dust remover is respectively connected with the pyrolysis gas inlet of the heating device, the pyrolysis gas inlet of the burnout chamber and the pyrolysis gas inlet of the pyrolysis gas purification system, the pyrolysis gas outlet of the heating device is connected with the pyrolysis gas inlet of the last-stage spiral pyrolysis device, the pyrolysis gas outlet of the last-stage spiral pyrolysis device is connected with the pyrolysis gas inlet of the last-stage spiral pyrolysis device, the pyrolysis gas outlets of the spiral pyrolysis devices are respectively connected with the pyrolysis gas inlet of the first-stage spiral pyrolysis device, and the pyrolysis gas outlet of the first-stage spiral pyrolysis device is connected with the pyrolysis gas inlet of the anaerobic pyrolysis device; an organic solid waste outlet of the anaerobic cracking device is connected with an organic solid waste inlet of the first-stage spiral cracking device, an organic solid waste outlet of the first-stage spiral cracking device is connected with an organic solid waste inlet of the next-stage spiral cracking device, and organic solid waste outlets of the spiral cracking devices are respectively connected with an organic solid waste inlet of the next-stage spiral cracking device; a flue gas outlet of the anaerobic cracking device is connected with a flue gas treatment system; the smoke outlet of the burnout chamber is connected with an oxygen-free cracking device.
The cracking system of the utility model comprises an anaerobic cracking device and a multi-stage spiral cracking unit, wherein each movable part of the multi-stage spiral cracking unit is provided with a sealing device, so as to prevent air from entering the multi-stage spiral unit to participate in reaction; the cracking system is in an anaerobic state in the cracking process, so that harmful gases such as dioxin and the like can not be generated, organic solid waste is heated in an anaerobic cracking device, moisture in the organic solid waste is gasified and discharged, most of generated cracking gas is sent to a heating device after dust removal treatment, and the rest part of the generated cracking gas is respectively sent to a burnout chamber and a cracking gas purification system. Pyrolysis gas heated by the heating device enters from the bottom of the spiral cracking device at the last stage, and sequentially enters the spiral cracking device at the first stage and the oxygen-free cracking device from bottom to top from the spiral cracking device at the last stage, so that the circulation of the pyrolysis gas is realized. Organic solid waste in the multistage spiral cracking device is continuously mixed and contacted with pyrolysis gas in the multistage spiral cracking device under the rotation and stirring of a continuously rotating spiral blade, and the organic solid waste is decomposed into micromolecular combustible substances under the action of the pyrolysis gas; and discharging the ash slag generated by cracking through a discharge hole of the last stage of spiral cracking device.
It should be noted that the pyrolysis gas flows in the opposite direction to the organic solid waste. The multi-stage spiral cracking unit can use a spiral structure, and can also use multi-stage series connection. The cracking system is operated under negative pressure, which aggravates the evaporation on the surface and inside of the material.
The heating system comprises a dust remover, a heating device and a burnout chamber. The pyrolysis gas discharged from the pyrolysis system contains a small amount of dust particles, and the dust in the pyrolysis gas is collected and captured by arranging a dust remover, so that the pyrolysis gas is primarily purified, and the operating pressure of a rear-end device is reduced. And a part of the pyrolysis gas enters the burnout chamber, the pyrolysis gas is combusted, and the generated flue gas is used for heating organic solid waste in the anaerobic cracking device, so that the aims of energy conservation and environmental protection are fulfilled. And the other part of the pyrolysis gas enters a heating device, and after being heated to 600 ℃, the pyrolysis gas returns to the cracking system again through a final-stage spiral cracking device to be used as an organic solid waste direct heating working medium. And leading the rest of the cracked gas to a cracked gas purification system, and storing the purified cracked gas for later use.
The main product of the traditional organic solid waste cracking process is an oil product, but the organic solid waste cracking oil has complex and unstable properties, and the product has no relevant standard. The utility model discloses a pyrolysis is organic useless admittedly, and the schizolysis product is the micromolecular cracked gas mainly, and the cracked gas indicates that the major component is H2、CO、CH4And C2H6Lower molecular weight compounds, more preferablyIs environment-friendly.
Further, the anaerobic cracking device comprises a cracking furnace and a jacket device, wherein the jacket device is arranged outside the cracking furnace, and a sealed space is formed between the jacket device and the cracking furnace and is a channel for heating a medium; the smoke outlet of the burnout chamber is connected with the smoke inlet of the jacket device. The high-temperature flue gas generated by the burnout chamber can pass through the heat exchanger to preheat air, then is led to the jacket device to indirectly heat organic solid waste, and the residual flue gas enters the flue gas treatment system.
Furthermore, the pyrolysis gas purification system comprises a deacidification device, a gas-water separator and a pyrolysis gas collection device which are sequentially connected.
The method comprises the following steps of removing most of acid gas hydrogen chloride and residual small amount of tar and carbon powder in a deacidification device, wherein the deacidification device can be provided with a multi-stage deacidification tower to ensure that impurities such as acid harmful gas in the pyrolysis gas are completely removed, then enabling the acid harmful gas to enter a gas-water separator, removing water, collecting clean and dry pyrolysis gas through a pyrolysis gas collecting device, and storing the clean and dry pyrolysis gas for later use.
As an embodiment, the device also comprises a cracked gas power generation device, and the cracked gas power generation device is connected with the cracked gas purification system. Specifically, the cracked gas power generation device can also be applied to devices which need electricity in the system. Generating power by using the purified cracked gas, and using the power by itself or combining the power with the power; the high-temperature flue gas generated by the power generation device can be sent to the jacket device, and the oxygen-free cracking device is heated by utilizing the waste heat of the flue gas, so that the energy consumption can be reduced, and the waste is avoided. And the heating device can also adopt an electric heating mode to heat the cracked gas.
Generally, a torch can be also arranged, and if the cracked gas in the cracked gas collecting device needs to be discharged emergently, the cracked gas can be discharged by burning the torch and is placed to overflow to pollute the environment.
Still further, the spiral structure of the spiral cracking unit is one or more of a single spiral, a double spiral and a shaftless spiral.
A process for treating a system of organic solid waste comprising the steps of:
firstly, organic solid waste is sent to an anaerobic cracking device, the organic solid waste is heated in the front section and evaporated to discharge redundant moisture, and the rear section generates cracking gas under the action of high temperature; cracking gas generated in the cracking process of the anaerobic cracking device is led to a dust remover; the flue gas discharged by the anaerobic cracking device is led to a flue gas treatment system for treatment;
2) the pyrolysis gas subjected to dust removal treatment in the step 1) has three directions, wherein one part of the pyrolysis gas is sent to a heating device, one part of the pyrolysis gas is sent to a burnout chamber, and the other part of the pyrolysis gas is sent to a pyrolysis gas purification system; pyrolysis gas heated by the heating device enters from the bottom of the last-stage spiral cracking device through a pipeline, and sequentially passes through the last-stage spiral cracking device, the primary spiral cracking device and the anaerobic cracking device from bottom to top; discharging the organic solid waste in the step 1) from the anaerobic cracking device, and then sequentially entering a primary spiral cracking device and a final spiral cracking device from top to bottom;
3) the pyrolysis gas sent to the burnout chamber in the step 2) is completely combusted in the burnout chamber, and the formed flue gas is discharged to an oxygen-free cracking device for heating organic solid waste; the pyrolysis gas sent to the pyrolysis gas purification system in the step 2) is purified and stored for later use.
Further, in the step 1), the temperature of the pyrolysis gas sent to the first-stage spiral cracking device is 550-650 ℃.
Still further, in the step 1), the temperature of the pyrolysis gas sent from the anaerobic pyrolysis device to the dust remover is 150-200 ℃, and preferably 160 ℃.
Compared with the prior art, the beneficial effects of the utility model reside in that:
(1) the system for recovering organic solid waste of the utility model adopts an anaerobic cracking technology, so that pollutants of dioxin can not be generated in the cracking process, and the cracked product is mainly micromolecular cracking gas, so that the use is more environment-friendly; the pyrolysis gas of the organic solid waste raw material is used as a heating working medium, and the pyrolysis gas is recycled by the heating device, so that the heat exchange efficiency is increased, and the pyrolysis efficiency is improved.
(2) The utility model discloses a pyrolysis gas is direct to the heating of organic solid waste material, and indirect heating raw materials is retrieved to produced high temperature flue gas of in-process, and the subregion reaction effectively promotes heat utilization efficiency.
Drawings
FIG. 1 is a connection diagram of the apparatus of example 1;
FIG. 2 is a connection diagram of the apparatus of example 2;
FIG. 3 is a diagram showing the connection of the apparatus of example 3.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and the detailed description, and it should be noted that the embodiments or technical features described below can be arbitrarily combined to form a new embodiment without conflict.
Example 1
A system for treating organic solid waste is shown in figure 1 and comprises a cracking system, a heat supply system, a cracking gas purification system and a flue gas treatment system; the cracking system comprises an oxygen-free cracking device and a multi-stage spiral cracking unit, wherein the multi-stage spiral cracking unit is provided with a sealing device and comprises a first-stage spiral cracking device and a second-stage spiral cracking device; the heating system comprises a dust remover, a burnout chamber and a heating device;
a pyrolysis gas outlet of the anaerobic pyrolysis device is connected with a pyrolysis gas inlet of the dust remover; a pyrolysis gas outlet of the dust remover is respectively connected with a pyrolysis gas inlet of the heating device, a pyrolysis gas inlet of the burnout chamber and a pyrolysis gas inlet of the pyrolysis gas purification system, a pyrolysis gas outlet of the heating device is connected with a pyrolysis gas inlet of the secondary spiral cracking device, a pyrolysis gas outlet of the secondary spiral cracking device is connected with a pyrolysis gas inlet of the primary spiral cracking device, and a pyrolysis gas outlet of the primary spiral cracking device is connected with a pyrolysis gas inlet of the anaerobic cracking device; an organic solid waste outlet of the anaerobic cracking device is connected with an organic solid waste inlet of the primary spiral cracking device, and an organic solid waste outlet of the primary spiral cracking device is connected with an organic solid waste inlet of the secondary spiral cracking device; a flue gas outlet of the anaerobic cracking device is connected with a flue gas treatment system; the smoke outlet of the burnout chamber is connected with an oxygen-free cracking device.
A process for treating a system of organic solid waste comprising the steps of:
1) firstly, conveying organic solid waste to an anaerobic cracking device, heating the organic solid waste to generate high-temperature cracking gas, and discharging redundant moisture; the anaerobic cracking device conveys the cracking gas with the temperature of 160 ℃ to a dust remover to lead to the dust remover; the flue gas discharged by the anaerobic cracking device is led to a flue gas treatment system for treatment;
2) the pyrolysis gas subjected to dust removal treatment in the step 1) has three directions, wherein one part of the pyrolysis gas is sent to a heating device, one part of the pyrolysis gas is sent to a burnout chamber, and the other part of the pyrolysis gas is sent to a pyrolysis gas purification system; pyrolysis gas heated to 600 ℃ by the heating device enters from the bottom of the secondary spiral cracking device through a pipeline, and the pyrolysis gas sequentially passes through the secondary spiral cracking device, the primary spiral cracking device and the anaerobic cracking device from bottom to top; discharging the organic solid waste in the step 1) from the anaerobic cracking device, and then sequentially entering a primary spiral cracking device and a secondary spiral cracking device from top to bottom;
3) the pyrolysis gas sent to the burnout chamber in the step 2) is completely combusted in the burnout chamber, and the formed flue gas is discharged to an oxygen-free cracking device for heating organic solid waste; the pyrolysis gas sent to the pyrolysis gas purification system in the step 2) is purified and then stored in a gas cache tank for later use.
Example 2
A system for treating organic solid waste is shown in figure 2 and comprises a cracking system, a heat supply system, a cracking gas purification system, a flue gas treatment system and a cracking gas power generation device; the cracking system comprises an oxygen-free cracking device and a multi-stage spiral cracking unit, wherein the multi-stage spiral cracking unit is provided with a sealing device and comprises a first-stage spiral cracking device, a second-stage spiral cracking device and a third-stage spiral device; the heating system comprises a dust remover, a burnout chamber and a heating device; the anaerobic cracking device comprises a cracking furnace and a jacket device, wherein the jacket device is arranged outside the cracking furnace; specifically, the jacket device is of a double-layer jacket structure, and is further provided with a flue gas discharge port and a feeding push rod which are directly communicated with the cavity of the cracking furnace, and the discharge port and the pyrolysis gas outlet are arranged at the tail end of the jacket device. The pyrolysis gas purification system comprises a deacidification device (a first deacidification tower and a second deacidification tower), a gas-water separator, a pyrolysis gas collection device and a pyrolysis gas power generation device which are sequentially connected; the flue gas outlet of the cracking gas power generation device and the flue gas outlet of the burnout chamber are connected with the jacket device.
A pyrolysis gas outlet of the pyrolysis furnace is connected with a pyrolysis gas inlet of the dust remover; a pyrolysis gas outlet of the dust remover is respectively connected with a pyrolysis gas inlet of the heating device, a pyrolysis gas inlet of the burnout chamber and a pyrolysis gas inlet of the pyrolysis gas purification system, a pyrolysis gas outlet of the heating device is connected with a pyrolysis gas inlet of the third-level spiral cracking device, a pyrolysis gas outlet of the third-level spiral cracking device is connected with a pyrolysis gas inlet of the second-level spiral cracking device, a pyrolysis gas outlet of the second-level spiral cracking device is connected with a pyrolysis gas inlet of the first-level spiral cracking device, and a pyrolysis gas outlet of the first-level spiral cracking device is connected with a pyrolysis gas inlet of the cracking furnace; an organic solid waste outlet of the cracking furnace is connected with an organic solid waste inlet of the primary spiral cracking device, an organic solid waste outlet of the primary spiral cracking device is connected with an organic solid waste inlet of the secondary spiral cracking device, and an organic solid waste outlet of the secondary spiral cracking device is connected with an organic solid waste inlet of the tertiary spiral cracking device; the flue gas outlet of the cracking furnace is connected with a flue gas treatment system.
A process for treating a system of organic solid waste comprising the steps of:
1) firstly, organic solid waste is sent to a cracking furnace through a push rod, the organic solid waste is heated to generate high-temperature cracking gas, and redundant moisture is discharged; the cracking furnace conveys the cracking gas with the temperature of 160 ℃ to a dust remover to lead to the dust remover; the flue gas discharged by the cracking furnace is led to a flue gas treatment system for treatment;
2) the pyrolysis gas subjected to dust removal treatment in the step 1) has three directions, most (more than 85%) of the pyrolysis gas is sent to a heating device for cyclic heating, one part of the pyrolysis gas is sent to a burnout chamber, and the other part of the pyrolysis gas is sent to a pyrolysis gas purification system; pyrolysis gas heated to 550 ℃ by the heating device enters from the bottom of the three-stage spiral cracking device through a pipeline, and sequentially passes through the three-stage spiral cracking device, the two-stage spiral cracking device, the one-stage spiral cracking device and the cracking furnace from bottom to top; discharging the organic solid waste in the step 1) from the cracking furnace, and then sequentially entering a primary spiral cracking device, a secondary spiral cracking device and a tertiary spiral cracking device from top to bottom;
3) the pyrolysis gas sent to the burnout chamber in the step 2) is completely combusted in the burnout chamber to form high-temperature flue gas at 1100-1150 ℃, and most of the high-temperature flue gas is led to a jacket device and is used for indirectly heating the cracking furnace;
7) the pyrolysis gas sent to the pyrolysis gas purification system in the step 2) enters a first-stage deacidification tower and then enters a second-stage deacidification tower, then enters a gas-water separator, after moisture is removed, the clean and dry pyrolysis gas is led to a gas buffer tank for storage, and then the pyrolysis gas in the gas buffer tank is sent to a pyrolysis gas power generation device to be converted into electric energy which can be used by the device in the embodiment. And the flue gas generated by the pyrolysis gas power generation device is led to the jacket device to heat the pyrolysis furnace.
Example 3
A system for recycling organic solid waste and treating the organic solid waste, as shown in figure 3, comprises a boiler, a cracking system, a heat supply system, a cracked gas purification system and a flue gas treatment system; the cracking system comprises an oxygen-free cracking device and a multi-stage spiral cracking unit, wherein the multi-stage spiral cracking unit is provided with a sealing device and comprises a first-stage spiral cracking device and a second-stage spiral cracking device; the heating system comprises a dust remover, a burnout chamber and a heating device; the anaerobic cracking device comprises a cracking furnace and a jacket device, wherein the jacket device is arranged outside the cracking furnace; specifically, the jacket device is of a double-layer jacket structure, and is further provided with a waste gas and flue gas discharge port and a feeding push rod which are directly communicated with the cavity of the cracking furnace, and the discharge port and the pyrolysis gas outlet are arranged at the tail end of the jacket device. A pyrolysis gas inlet of the boiler is connected with a pyrolysis gas outlet of the pyrolysis gas purification system; the flue gas outlet of the boiler is connected with the high-temperature flue gas inlet of the jacket device; the flue gas outlet of the cracking gas power generation device and the flue gas outlet of the burnout chamber are connected with the jacket device.
The pyrolysis gas purification system comprises a deacidification device (a first deacidification tower and a second deacidification tower), a gas-water separator, a pyrolysis gas collection device and a pyrolysis gas power generation device which are sequentially connected;
a pyrolysis gas outlet of the pyrolysis furnace is connected with a pyrolysis gas inlet of the dust remover; a pyrolysis gas outlet of the dust remover is respectively connected with a pyrolysis gas inlet of the heating device, a pyrolysis gas inlet of the burnout chamber and a pyrolysis gas inlet of the pyrolysis gas purification system, a pyrolysis gas outlet of the heating device is connected with a pyrolysis gas inlet of the secondary spiral cracking device, a pyrolysis gas outlet of the secondary spiral cracking device is connected with a pyrolysis gas inlet of the primary spiral cracking device, and a pyrolysis gas outlet of the primary spiral cracking device is connected with a pyrolysis gas inlet of the anaerobic cracking device; an organic solid waste outlet of the anaerobic cracking device is connected with an organic solid waste inlet of the primary spiral cracking device, and an organic solid waste outlet of the primary spiral cracking device is connected with an organic solid waste inlet of the secondary spiral cracking device; a flue gas outlet of the anaerobic cracking device is connected with a flue gas treatment system; the smoke outlet of the burnout chamber is connected with an oxygen-free cracking device.
The process of the system for treating organic solid waste by the system for recycling organic solid waste comprises the following steps:
1) flue gas at 200-550 ℃ discharged by burning pyrolysis gas by a boiler is sent to a jacket device outside the pyrolysis furnace and used for heating organic solid waste in the pyrolysis furnace; sending the organic solid waste to a cracking furnace, heating the organic solid waste to generate high-temperature cracking gas, and discharging redundant moisture; the cracking furnace conveys the cracking gas with the temperature of 160 ℃ to a dust remover to lead to the dust remover; the waste gas and the flue gas discharged by the cracking furnace are led to a flue gas treatment system for treatment;
2) the pyrolysis gas subjected to dust removal treatment in the step 1) has three directions, most (more than 85%) of the pyrolysis gas is sent to a heating device, one part of the pyrolysis gas is sent to a burnout chamber, and the other part of the pyrolysis gas is sent to a pyrolysis gas purification system; pyrolysis gas heated to 650 ℃ by the heating device enters from the bottom of the secondary spiral cracking device through a pipeline, and the pyrolysis gas sequentially passes through the secondary spiral cracking device, the primary spiral cracking device and the cracking furnace; discharging the organic solid waste in the step 1) from the anaerobic cracking device, and sequentially entering a primary spiral cracking device and a secondary spiral cracking device;
3) the pyrolysis gas sent to the burnout chamber in the step 2) is completely combusted in the burnout chamber to form high-temperature flue gas at 1100-1150 ℃, and most of the high-temperature flue gas is led to a jacket device and is used for indirectly heating the cracking furnace;
7) the pyrolysis gas sent to the pyrolysis gas purification system in the step 2) enters a first-stage deacidification tower, then enters a second-stage deacidification tower, then enters a gas-water separator, after moisture is removed, the clean and dry pyrolysis gas is led to a gas buffer tank for storage, and then the pyrolysis gas in the gas buffer tank is sent to a pyrolysis gas power generation device to be converted into electric energy for use by the device in the embodiment. And the flue gas generated by the pyrolysis gas power generation device is led to the jacket device to heat the pyrolysis furnace.
The above embodiments are only preferred embodiments of the present invention, and the protection scope of the present invention cannot be limited thereby, and any insubstantial changes and substitutions made by those skilled in the art based on the present invention are all within the protection scope of the present invention.
Claims (6)
1. A system for treating organic solid waste is characterized by comprising a cracking system, a heat supply system, a cracking gas purification system and a flue gas treatment system; the cracking system comprises an oxygen-free cracking device and a multi-stage spiral cracking unit, wherein the multi-stage spiral cracking unit is provided with a sealing device and is at least a two-stage spiral cracking device; the heating system comprises a dust remover, a burnout chamber and a heating device;
a pyrolysis gas outlet of the anaerobic pyrolysis device is connected with a pyrolysis gas inlet of the dust remover; the pyrolysis gas outlet of the dust remover is respectively connected with the pyrolysis gas inlet of the heating device, the pyrolysis gas inlet of the burnout chamber and the pyrolysis gas inlet of the pyrolysis gas purification system, the pyrolysis gas outlet of the heating device is connected with the pyrolysis gas inlet of the last-stage spiral pyrolysis device, the pyrolysis gas outlet of the last-stage spiral pyrolysis device is connected with the pyrolysis gas inlet of the last-stage spiral pyrolysis device, the pyrolysis gas outlets of the spiral pyrolysis devices are respectively connected with the pyrolysis gas inlet of the first-stage spiral pyrolysis device, and the pyrolysis gas outlet of the first-stage spiral pyrolysis device is connected with the pyrolysis gas inlet of the anaerobic pyrolysis device; an organic solid waste outlet of the anaerobic cracking device is connected with an organic solid waste inlet of the first-stage spiral cracking device, an organic solid waste outlet of the first-stage spiral cracking device is connected with an organic solid waste inlet of the next-stage spiral cracking device, and organic solid waste outlets of the spiral cracking devices are respectively connected with an organic solid waste inlet of the next-stage spiral cracking device; a flue gas outlet of the anaerobic cracking device is connected with a flue gas treatment system; the smoke outlet of the burnout chamber is connected with an oxygen-free cracking device.
2. The system for treating organic solid waste of claim 1, wherein the anaerobic cracking device comprises a cracking furnace and a jacket device, the jacket device is arranged outside the cracking furnace, and a sealed space is formed between the jacket device and the cracking furnace and is used as a channel for heating media; the smoke outlet of the burnout chamber is connected with the smoke inlet of the jacket device.
3. The system for treating organic solid waste of claim 2, further comprising a boiler, wherein a cracked gas inlet of the boiler is connected with a cracked gas outlet of the cracked gas purification system; and a high-temperature flue gas outlet of the boiler is connected with the jacket device.
4. The system for treating organic solid waste of claim 1, further comprising a cracked gas power generation device connected to the cracked gas purification system.
5. The system for treating organic solid waste according to claim 1, wherein the pyrolysis gas purification system comprises a deacidification device, a gas-water separator, a pyrolysis gas collection device and a pyrolysis gas power generation device which are connected in sequence.
6. The system for treating organic solid waste of claim 1, wherein the spiral structure of the multi-stage spiral cracking device is one or more of a single spiral, a double spiral and a shaftless spiral.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022858390.XU CN214937226U (en) | 2020-12-01 | 2020-12-01 | System for handle organic solid useless |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022858390.XU CN214937226U (en) | 2020-12-01 | 2020-12-01 | System for handle organic solid useless |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214937226U true CN214937226U (en) | 2021-11-30 |
Family
ID=79035963
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022858390.XU Active CN214937226U (en) | 2020-12-01 | 2020-12-01 | System for handle organic solid useless |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214937226U (en) |
-
2020
- 2020-12-01 CN CN202022858390.XU patent/CN214937226U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105737163B (en) | Household garbage low-temperature pyrolysis system and method based on decoupling combustion | |
| CN106493148A (en) | A kind of solid organic castoff gasification and melting circulating disposal process | |
| CN102746903B (en) | Large-scale domestic garbage dry distillation and gasification furnace without exhaust gas or dioxin emission | |
| CN109899800A (en) | Based on the compound thermal cracking gasification treatment process of house refuse and system | |
| CN203265240U (en) | Device for preparing fuel gas by utilizing domestic garbage and generating power by utilizing fuel gas | |
| CN107513389B (en) | Carbonizing device capable of treating garbage | |
| CN106590702B (en) | A kind of house refuse low temperature pyrogenation electricity generation system and method | |
| CN204388069U (en) | A kind of solid waste pyrolysis formula fusion and gasification treating apparatus | |
| CN106734080A (en) | The system and method for processing solid waste | |
| CN205316329U (en) | Portable rural garbage pyrolytic gasification equipment | |
| CN106433799A (en) | System and method for disposing household garbage | |
| CN203265244U (en) | Equipment for fuel gas preparation and gas power generation by virtue of household garbage | |
| CN109028079B (en) | System for pyrolysis and gasification of biomass waste and cascade utilization of waste heat thereof | |
| CN109513730A (en) | A kind of solid organic castoff vacuum pyrolysis System and method for | |
| CN112735625A (en) | Equipment and process for treating organic matters by utilizing heat carrier | |
| CN105351019A (en) | Power generation technique based on pyrolyzation and gasification of refuse derived fuel (RDF) prepared from household refuse and incineration of fuel gas | |
| CN203669943U (en) | Energy-saving power generation device by using solid wastes | |
| CN204114952U (en) | RDF burning electricity generation system prepared by a kind of clean and effective rubbish | |
| CN206449652U (en) | A kind of house refuse low temperature pyrogenation electricity generation system | |
| CN112708428A (en) | System and process for treating organic solid waste | |
| CN206405159U (en) | The system for handling solid waste | |
| CN207756595U (en) | A kind of electricity generation system of debirs clean utilization | |
| CN214937226U (en) | System for handle organic solid useless | |
| CN206143142U (en) | System for handle domestic waste | |
| CN211871883U (en) | Range-dividing domestic garbage drying pyrolysis purification technology |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |