CN109357261B - Organic matter solid waste treatment equipment - Google Patents
Organic matter solid waste treatment equipment Download PDFInfo
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- CN109357261B CN109357261B CN201811551225.0A CN201811551225A CN109357261B CN 109357261 B CN109357261 B CN 109357261B CN 201811551225 A CN201811551225 A CN 201811551225A CN 109357261 B CN109357261 B CN 109357261B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/302—Treating pyrosolids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/303—Burning pyrogases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
- F23G2206/203—Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The embodiment of the invention discloses organic matter solid waste treatment equipment, which comprises a reactor and a purification tower communicated with the reactor; the purification tower is communicated with an alkali liquor tank and a gas compressor; the gas compressor is communicated with a gas storage cabinet which is communicated with a gas generator; the exhaust end of the gas generator is communicated with the reactor, and the output end of the gas generator is connected with an electric appliance; the biomass garbage is reacted to generate combustible gas for power generation of the gas generator through the reactor, and high-temperature carbon dioxide generated by the gas generator can enter the reactor for catalytic reaction, so that the biological garbage can be recycled, the generation of the garbage is reduced, the quality of the living environment is improved, the garbage is utilized for power generation, and reaction products have useful values; the garbage is not required to be delivered, the garbage is utilized to generate electricity, the generation of the garbage is greatly reduced, the cost is saved, the energy is saved, the public interest is improved, and the garbage can is suitable for popularization and use.
Description
Technical Field
The embodiment of the invention relates to the technical field of mechanical equipment, in particular to organic matter solid waste treatment equipment.
Background
Along with the development of society, the quality of human life is continuously improved, the human material life is increasingly enriched, the amount of garbage manufactured in human life is also continuously increased, the increase of the garbage not only causes bad influence on the human living environment, but also causes a great amount of loss on resources; according to statistics, more than 80% of the solid waste is organic waste; these organic (biomass) wastes are treated the same as the other wastes; not only wasting resources but also polluting environment.
Disclosure of Invention
Therefore, the embodiment of the invention provides organic solid waste treatment equipment, which aims to solve the problems of resource waste and environmental pollution caused by the fact that solid organic waste is continuously increased due to the fact that human living materials are increasingly enriched in daily life materials in the prior art.
In order to achieve the above object, an embodiment of the present invention provides the following:
In a first aspect of embodiments of the present invention, there is provided an organic matter solid waste treatment apparatus comprising a reactor and a purification tower in communication with the reactor; the purification tower is communicated with an alkali liquor tank and a gas compressor; the gas compressor is communicated with a gas storage cabinet, and the gas storage cabinet is communicated with a gas generator; the gas generator exhaust end is communicated with the reactor, and the output end of the gas generator is connected with an electric appliance.
Further, the reactor comprises a tank body, and the interior of the tank body is divided into a crushing area, a main reaction area and a transition area through two pore plates; a material inlet is formed in one side of the top of the crushing area, and a valve is arranged on the material inlet; a garbage crusher is arranged in the crushing area; the top of the crushing area is communicated with a catalyst tank through a valve; one side of the top of the main reaction zone is communicated with the exhaust end of the gas generator through a pipeline;
the bottom of the transition region is communicated with a combustion chamber through a necking pipe; the outer side of the combustion chamber is hermetically connected with a jacket; the jacket is communicated with a condensate pipe through a valve; the jacket is connected with a water pump through a pipeline, and the output end of the water pump is communicated with a water tank;
One side of the necking pipe is connected with a ventilator through an air pipeline; the top of the jacket is communicated with a steam pipeline through a valve, and one end of the steam pipeline is communicated with the necking pipe.
Further, an arc-shaped plate is fixedly connected to the inner wall of one side of the reducing pipe, and gaps are reserved between two ends of the arc-shaped plate and the inner walls of the left end and the right end of the reducing pipe respectively; one end of the air pipeline extends to the inside of the necking pipe, and the port of the air pipeline is bent upwards and is positioned right below the arc-shaped plate; one end of the steam pipeline extends to the inside of the necking pipe, and the port of the steam pipeline is bent downwards to be positioned right above the arc-shaped plate.
Furthermore, the top surface of the arc-shaped plate is convex, and the bottom surface of the arc-shaped plate is concave.
Furthermore, one side of the necking pipe is communicated with an oil pump through a pipeline, and the output end of the oil pump is communicated with the main reaction area through a pipeline.
further, one side of the bottom of the combustion chamber is communicated with a gas conveyer; the output end of the gas conveyer is communicated with the catalyst tank through a pipeline.
Further, one side of the bottom of the purifying tower is communicated with one side of the top of the reactor through a pipeline; the top of the purification tower is communicated with the gas compressor through a pipeline.
Further, the bottom of the purification tower is communicated with a liquid storage tank.
Further, the bottom of the lye tank is communicated with a lye pump through a pipeline, and the output end of the lye pump is communicated with one side of the top of the purification tower through a lye pipeline; a dosing port is arranged on one side of the alkali liquor tank; the top of the alkali liquor tank is communicated with a water pipe through a valve.
Furthermore, one end of the alkali liquor tank way extends to the inside of the purification tower, and a port of the alkali liquor tank way is communicated with a nozzle with a downward nozzle.
According to the embodiment of the invention, the organic solid waste treatment equipment has the following advantages: the biomass garbage is reacted to generate combustible gas for power generation of the gas generator through the reactor, and high-temperature carbon dioxide generated by the gas generator can enter the reactor for catalytic reaction, so that the biological garbage can be recycled, the generation of the garbage is reduced, the quality of the living environment is improved, the garbage is utilized for power generation, and reaction products have useful values; the product generated by the purifying tower can be used as a cleaning agent, the gas generated after purification can be used as the fuel of a fuel generator, and the electric energy generated by the generator can be stored in an electric appliance for standby; the condensed water in the jacket is heated by the heat of the combustion chamber reaction area and the combustion chamber to form hot water which is stored in the water tank for use; the garbage is not sent out, the garbage is used for generating electricity, the garbage production is greatly reduced, the cost is saved, the energy is saved, the integrated technology of organic matter pyrolysis, carbon gasification and gas power generation is realized, the public interest is improved, and the garbage power generation device is suitable for popularization and use.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. It should be apparent that the drawings in the following description are merely exemplary, and that other embodiments can be derived from the drawings provided by those of ordinary skill in the art without inventive effort.
The structures, ratios, sizes, and the like shown in the present specification are only used for matching with the contents disclosed in the specification, so as to be understood and read by those skilled in the art, and are not used to limit the conditions that the present invention can be implemented, so that the present invention has no technical significance, and any structural modifications, changes in the ratio relationship, or adjustments of the sizes, without affecting the effects and the achievable by the present invention, should still fall within the range that the technical contents disclosed in the present invention can cover.
Fig. 1 is a schematic view of an overall structure of an organic solid waste treatment apparatus according to an embodiment of the present invention.
In the figure: the device comprises a reactor 1, a purification tower 2, an alkali liquor tank 3, a gas compressor 4, a gas storage cabinet 5, a gas generator 6, the gas generator 6, an electric appliance 7, a pore plate 101, a crushing area 11, a main reaction area 12, a transition area 13, a material inlet 15, a garbage crusher 14, a catalyst tank 16, a necking pipe 17, a combustion chamber 8, a jacket 81, a condensate pipe 83, a water pump 85, a water tank 86, an air pipeline 19, a fan 110, a steam pipeline 84, an arc-shaped plate 18, an oil pump 87, a gas conveyor 82, a liquid storage tank 21, an alkali liquor pump 31, an alkali liquor pipeline 32, a medicine feeding port 33 and a water pipe nozzle 35.
Detailed Description
The present invention is described in terms of particular embodiments, other advantages and features of the invention will become apparent to those skilled in the art from the following disclosure, and it is to be understood that the described embodiments are merely exemplary of the invention and that it is not intended to limit the invention to the particular embodiments disclosed. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the present specification, the terms "upper", "lower", "left", "right", "middle", and the like are used for clarity of description only, and are not intended to limit the scope of the present invention, and changes or modifications in the relative relationship therebetween may be regarded as the scope of the present invention without substantial changes in the technical contents.
referring to fig. 1, the organic solid waste treatment equipment provided by the embodiment of the present invention includes a reactor 1 and a purification tower 2 communicated with the reactor 1; the purification tower 2 is communicated with an alkali liquor tank 3 and a gas compressor 4; the gas compressor 4 is communicated with a gas storage cabinet 5, and the gas storage cabinet 5 is communicated with a gas generator 6; the exhaust end of the gas generator 6 is communicated with the reactor 1, and the output end of the gas generator 6 is connected with an electric appliance 7; the reactor 1 comprises a tank body and passes through two pore plates 101, wherein a through hole on the pore plate at the bottom of the crushing zone is larger than a through hole on the pore plate at the bottom of the main reaction zone, materials can leak to the main reaction zone after being crushed to a certain degree in the crushing zone, products after reaction in the main reaction zone leak from the pore plate, and the purpose of the through hole of the pore plate is to prevent the materials from flowing downwards without being reacted; the inner part of the tank body is divided into a crushing zone 11, a main reaction zone 12 and a transition zone 13, and the division has the function of clear internal work and ensures that the work is orderly carried out; a material inlet 15 is formed in one side of the top of the crushing area 11, and a valve is arranged on the material inlet 15; a garbage crusher 14 is arranged in the crushing area 11; the top of the crushing area 11 is communicated with a catalyst tank 16 through a valve; one side of the top of a main reaction zone 12 is communicated with an exhaust end of a gas generator 6 through a pipeline, a microwave magnetron can be arranged in the main reaction zone to improve heat energy required by the reaction, the microwave is utilized to generate molecular vibration to promote pyrolysis reaction, spherical packing can be placed in the reaction zone to promote organic matters to absorb microwave energy, products of the main reaction zone are solid carbon, heavy tar and fuel gas (CO, H2, methane, carbon 2, carbon 3, carbon 4 and the like), the generated gas flows to a purification tower through the pipeline, and the generated solid-liquid substances flow to a combustion chamber; the bottom of the transition zone 13 is communicated with a combustion chamber 8 through a reducing pipe 17, the bottom of the combustion chamber is provided with a valve communicated with the outside, and the valve is used for cleaning dust in the interior and can play a role of slow flow in the process that a product generated by the reaction of the main reactor flows to the combustion chamber through the communication of the reducing pipe, so that the combination efficiency of the reaction product and air and water vapor is improved, and the oxidation combustion efficiency of solid carbon particles and a catalyst for adsorbing heavy coke is improved; the outer side of the combustion chamber 8 is hermetically connected with a jacket 81; the jacket 81 is communicated with a condensate pipe 83 through a valve; the jacket 81 is connected with a water pump 85 through a pipeline, and the output end of the water pump 85 is communicated with a water tank 86; the utilization rate of heat energy is increased; one side of the reducing pipe 17 is communicated with a fan 110 through an air pipeline 19; the top of the jacket 81 is communicated with a steam pipeline 84 through a valve, and one end of the steam pipeline 84 is communicated with the reducing pipe 17; the condensed water in the jacket is arranged below the combustion chamber and the reaction zone (the heat generated in the reaction of the reaction zone reaches about five hundred degrees), and the condensed water can be heated to boiling, so that steam enters the reducing pipe through the steam pipeline, a proper redox environment is provided, more combustible gas is obtained, and the combustion efficiency of the combustion chamber is improved.
Optimally, the inner wall of one side of the reducing pipe 17 is fixedly connected with an arc-shaped plate 18, and gaps are reserved between two ends of the arc-shaped plate 18 and the inner walls of the left end and the right end of the reducing pipe 17 respectively; one end of the air pipeline 19 extends into the necking pipe 17, and the port is bent upwards and positioned right below the arc-shaped plate 18; one end of the steam pipeline 84 extends to the inside of the necking pipe 17, and the port is bent downwards and is positioned right above the arc-shaped plate 18; the arc plate 18 has a convex top surface and a concave bottom surface.
When the device is used, substances flow out from the gaps at the two ends of the arc-shaped plate, so that the downward flow speed of reaction products is reduced, and the slow flow effect of the reaction products is enhanced; the entering air is sprayed upwards and impacts on the slow flow plate, so that the air is uniformly sputtered around the slow flow plate, and the aim of uniformly fusing with reaction products is fulfilled; the purpose of the lower spraying arc plate of the steam pipeline is the same as that of the air pipeline; the purpose that the arc-shaped plate is convex and concave is to prevent the product from staying on the arc-shaped plate.
Optimally, one side of the reducing pipe 17 is communicated with an oil pump 87 through a pipeline, and the output end of the oil pump 87 is communicated with the main reaction zone 12 through a pipeline; the pipeline communicated with the oil pump is positioned above the steam pipeline.
The purpose is to adsorb the heavy tar, and convey the heavy tar back to the main reaction area for secondary reaction, so as to improve the reaction rate of the reaction; and simultaneously, the heavy tar is prevented from coking and blocking the pipeline.
Preferably, one side of the bottom of the combustion chamber 8 is communicated with a gas conveyer 82; the output end of the gas conveyer 82 is communicated with the catalyst tank 16 through a pipeline; the catalyst is conveyed back to the catalyst tank for next use, so that the cost is reduced.
Optimally, one side of the bottom of the purification tower 2 is communicated with one side of the top of the reactor 1 through a pipeline; the top of the purification tower 2 is communicated with a gas compressor 4 through a pipeline; the device body of the purification tower after purification is mainly combustible gas, and the combustible gas is stored in the gas storage cabinet after passing through the gas compressor to provide a fuel generator for the gas generator.
Optimally, the bottom of the purification tower 2 is communicated with a liquid storage tank 21; it can be used as detergent for storing and purifying substances generated during hair growth, mainly sodium bicarbonate.
Optimally, the bottom of the lye tank 3 is communicated with a lye pump 31 through a pipeline, and the output end of the lye pump 31 is communicated with one side of the top of the purification tower 2 through a lye pipeline 32; one side of the lye tank 3 is provided with a drug feeding port 33, and the drug is mainly NAOH; the top of the lye tank 3 is communicated with a water pipe 34 through a valve.
Optimally, one end of the alkali liquor tank guide 32 extends into the purification tower 2, and a nozzle 35 with a downward nozzle is communicated at the port; the alkali liquor is sprayed downwards so that the alkali liquor can be fully contacted with the gas conveyed by the reactor, and the reaction is more uniform and thorough.
When in use, the valves adopt electric valves and various pumps to be electrically connected with an intelligent controller; opening a valve of a material inlet, putting the organic garbage into a crushing area in the reactor, and then closing a feed valve; opening a water inlet valve of the lye tank, and adding NAOH or Na2CO3 or a mixture of the NAOH and the Na2CO3 according to a certain proportion; starting a power supply, starting a gas generator when the power supply is in initial reaction, wherein the initial energy is provided by external gas, and generating electricity to drive power equipment or store electric energy in an electric appliance; the flue gas discharged by the combustion of the gas generator is mainly carbon dioxide, and the temperature is between 450 ℃ and 550 ℃; starting an alkali liquor pump after the gas generator is started, and pumping alkali liquor in an alkali liquor tank into the purification tower; the gas generator works to generate high-temperature carbon dioxide and simultaneously charges an electric appliance; after high-temperature carbon dioxide enters the reactor for a set time, starting a pulverizer to pulverize the materials, discharging air in the system, manufacturing an oxygen-free environment, and providing pyrolysis reaction conditions of 400-500 ℃; opening a valve below the catalyst tank while the pulverizer operates, and adding a catalyst into the reactor; the crushed substances enter the main reaction zone through the orifice plate and react at high temperature, reaction products flow to the combustion chamber through the reducing pipe, and a charge level indicator electrically connected with the intelligent controller is arranged on the reducing pipe; when the level indicator detects that the set count is reached; the fan, the condensate water valve, the valve at the bottom of the combustion chamber and the valve on the steam pipeline are opened to enable air and steam to enter the necking pipe, and the steam inlet valve is opened to make incomplete oxidation conditions for the oxidation zone, so that excessive carbon dioxide is avoided being generated, CO and H2 are generated as much as possible, and the gas yield is increased.
After gas generated by reaction enters a purification tower, an alkaline washing tower washes CO2 and acidic impurities in organic matters, the main component of the medicament is sodium carbonate, the main component after reaction is sodium bicarbonate which can be used as a detergent for cleaning oil stains, or can be used as a cooling medium to be fed into a heat tracing jacket of a reactor to be heated and decomposed into CO2 and sodium carbonate, CO2 and water vapor are cooled in a water tank, CO2 is discharged, and at the beginning of the next operation period, condensed water flows into the heat stirring jacket to dissolve the sodium carbonate and then flows back to a medicament tank for alkaline washing of an adsorption tower, so that the medicament can be recycled, and the cost is reduced to the maximum extent; the purified combustible gas enters a gas compressor to be compressed and then is sent into a gas storage cabinet to be used by a gas generator.
When the pressure of the gas storage cabinet is raised to 0.005MP, a valve from the gas storage cabinet to the gas generator is opened, and an external gas valve is closed; when the liquid at the bottom of the purification tower reaches a set value, a valve from the bottom of the purification tower to the liquid storage tank is opened, and the liquid is stored in the liquid storage tank; when the pressure of the gas storage cabinet reaches 0.002MP, a valve of a gas generator of the gas storage cabinet is closed; closing the generator, closing the fan, the valve on the steam pipeline, the valve on the adsorbent tank, the valve at the bottom of the combustion chamber and the pulverizer; starting a water pump to convey hot water in the jacket into the water tank; when the water temperature reaches 40 ℃, closing the water pump and the condensed water inlet; starting a fan and a gas conveyor, oxidizing and combusting solid carbon particles generated in a reaction area and a catalyst adsorbing heavy coke, enabling the coked catalyst to fall into the bottom of a combustion chamber, conveying the coked catalyst to a catalyst tank by a gas conveyor after reaching a certain height, conveying the coked catalyst to a catalyst tank at the top by the gas conveyor, and if the storage amount of the catalyst tank is small, starting the gas conveyor to convey the catalyst back to the catalyst tank in the reaction process by material level control arranged on the catalyst tank so as to realize the recycling use of the catalyst and reduce the cost without external regeneration; after the conveying is finished, the fan and the gas conveyer are closed; at which point the operation is complete.
Although the invention has been described in detail above with reference to a general description and specific examples, it will be apparent to one skilled in the art that modifications or improvements may be made thereto based on the invention. Accordingly, such modifications and improvements are intended to be within the scope of the invention as claimed.
Claims (9)
1. The organic solid waste treatment equipment is characterized by comprising a reactor (1) and a purification tower (2) communicated with the reactor (1); the purification tower (2) is communicated with an alkali liquor tank (3) and a gas compressor (4); the gas compressor (4) is communicated with a gas storage cabinet (5), and the gas storage cabinet (5) is communicated with a gas generator (6); the exhaust end of the gas generator (6) is communicated with the reactor (1), and the output end of the gas generator (6) is connected with an electric appliance (7); the reactor (1) comprises a tank body, and the interior of the tank body is divided into a crushing area (11), a main reaction area (12) and a transition area (13) through two pore plates (101); a material inlet (15) is formed in one side of the top of the crushing area (11), and a valve is arranged on the material inlet (15); a garbage crusher (14) is arranged in the crushing area (11); the top of the crushing area (11) is communicated with a catalyst tank (16) through a valve; one side of the top of the main reaction zone (12) is communicated with the exhaust end of the gas generator (6) through a pipeline;
The bottom of the transition region (13) is communicated with a combustion chamber (8) through a necking pipe (17); the outer side of the combustion chamber (8) is hermetically connected with a jacket (81); the jacket (81) is communicated with a condensate pipe (83) through a valve; the jacket (81) is connected with a water pump (85) through a pipeline, and the output end of the water pump (85) is communicated with a water tank (86);
One side of the necking pipe (17) is communicated with a fan (110) through an air pipeline (19); the top of the jacket (81) is communicated with a steam pipeline (84) through a valve, and one end of the steam pipeline (84) is communicated with the necking pipe (17).
2. The organic solid waste treatment equipment according to claim 1, wherein an arc-shaped plate (18) is fixedly connected to the inner wall of one side of the reducing pipe (17), and gaps exist between two ends of the arc-shaped plate (18) and the inner walls of the left end and the right end of the reducing pipe (17) respectively; one end of the air pipeline (19) extends to the inside of the necking pipe (17), and the port of the air pipeline is bent upwards and is positioned right below the arc-shaped plate (18); one end of the steam pipeline (84) extends to the inside of the necking pipe (17), and a port of the steam pipeline is bent downwards and is positioned right above the arc-shaped plate (18).
3. The organic solid waste treatment equipment according to claim 2, wherein the arc-shaped plate (18) is convex on the top surface and concave on the bottom surface.
4. The organic solid waste treatment equipment according to claim 1, wherein one side of the reducing pipe (17) is communicated with an oil pump (87) through a pipeline, and the output end of the oil pump (87) is communicated with the main reaction zone (12) through a pipeline.
5. The organic solid waste treatment equipment according to claim 1, wherein a gas conveyor (82) is communicated with one side of the bottom of the combustion chamber (8); the output end of the gas conveyer (82) is communicated with the catalyst tank (16) through a pipeline.
6. The organic solid waste treatment equipment according to claim 1, wherein the bottom side of the purification tower (2) is communicated with the top side of the reactor (1) through a pipeline; the top of the purification tower (2) is communicated with the gas compressor (4) through a pipeline.
7. the organic solid waste treatment equipment according to claim 1, wherein the bottom of the purification tower (2) is communicated with a liquid storage tank (21).
8. The organic solid waste treatment equipment according to claim 1, wherein the bottom of the lye tank (3) is communicated with a lye pump (31) through a pipeline, and the output end of the lye pump (31) is communicated with one side of the top of the purification tower (2) through a lye pipeline (32); a drug feeding port (33) is arranged on one side of the alkali liquor tank (3); the top of the lye tank (3) is communicated with a water pipe (34) through a valve.
9. The organic solid waste treatment equipment according to claim 8, wherein one end of the alkali liquor tank (32) extends to the interior of the purification tower (2) and a port is communicated with a nozzle (35) with a downward nozzle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811551225.0A CN109357261B (en) | 2018-12-18 | 2018-12-18 | Organic matter solid waste treatment equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811551225.0A CN109357261B (en) | 2018-12-18 | 2018-12-18 | Organic matter solid waste treatment equipment |
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| CN109357261A CN109357261A (en) | 2019-02-19 |
| CN109357261B true CN109357261B (en) | 2019-12-17 |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103666505A (en) * | 2012-09-21 | 2014-03-26 | 周鼎力 | Equipment for reducing and transforming household garbage or organic waste into energy resources |
| CN104804771A (en) * | 2015-03-31 | 2015-07-29 | 李大鹏 | Device and method for clean coal gas power generation and cleaning fuel co-production |
| CN105351941A (en) * | 2014-08-20 | 2016-02-24 | 福建正仁环保有限公司 | Power generation technique based on pyrolyzation and gasification of household refuse and incineration of fuel gas |
| CN107435934A (en) * | 2017-04-05 | 2017-12-05 | 李艺 | A kind of house refuse continuously thermal, ashing environment-friendly processing unit |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6066809B2 (en) * | 2013-04-10 | 2017-01-25 | 三菱重工環境・化学エンジニアリング株式会社 | Biomass pyrolysis device and power generation system |
-
2018
- 2018-12-18 CN CN201811551225.0A patent/CN109357261B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103666505A (en) * | 2012-09-21 | 2014-03-26 | 周鼎力 | Equipment for reducing and transforming household garbage or organic waste into energy resources |
| CN105351941A (en) * | 2014-08-20 | 2016-02-24 | 福建正仁环保有限公司 | Power generation technique based on pyrolyzation and gasification of household refuse and incineration of fuel gas |
| CN104804771A (en) * | 2015-03-31 | 2015-07-29 | 李大鹏 | Device and method for clean coal gas power generation and cleaning fuel co-production |
| CN107435934A (en) * | 2017-04-05 | 2017-12-05 | 李艺 | A kind of house refuse continuously thermal, ashing environment-friendly processing unit |
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| CN109357261A (en) | 2019-02-19 |
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