CN214881023U - Livestock and poultry manure straw resourceful treatment device - Google Patents
Livestock and poultry manure straw resourceful treatment device Download PDFInfo
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- CN214881023U CN214881023U CN202120718392.0U CN202120718392U CN214881023U CN 214881023 U CN214881023 U CN 214881023U CN 202120718392 U CN202120718392 U CN 202120718392U CN 214881023 U CN214881023 U CN 214881023U
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Abstract
The utility model discloses a livestock and poultry excrement straw resourceful treatment device belongs to agricultural waste utilization field to it is discontinuous with aerobic fermentation production process to solve anaerobic fermentation, and the gas manure production disjointed scheduling problem. The utility model discloses technical scheme as follows: a livestock and poultry manure straw recycling treatment device comprises a continuous anaerobic dry fermentation device, an aerobic fermentation composting device and a continuous anaerobic wet fermentation device, wherein a discharge port of the continuous anaerobic dry fermentation device is connected with the aerobic fermentation composting device, and the continuous anaerobic wet fermentation device is arranged outside the aerobic fermentation composting device; the inner cavity of the continuous anaerobic dry fermentation device is provided with a spray pipeline, and a liquid storage tank of the continuous anaerobic wet fermentation device is connected with the spray pipeline through a liquid storage pipeline. The utility model discloses produce gas and aerobic fermentation compost with anaerobic fermentation and combine, realize the gas manure coproduction, not only effectively utilized the anaerobic fermentation residual, can give anaerobic fermentation with the heat transfer that aerobic fermentation produced again, reduce the energy consumption.
Description
Technical Field
The utility model belongs to agricultural waste utilizes the field, concretely relates to dirty straw resourceful treatment device of beasts and birds excrement.
Background
Agricultural rural waste in China has large output, various types and complex components. Anaerobic fermentation is an important way for producing renewable energy biogas by utilizing agricultural wastes, and mainly comprises wet anaerobic fermentation and dry anaerobic fermentation. The traditional wet anaerobic fermentation has large water consumption, can also produce a large amount of biogas slurry, and has low utilization rate of the biogas slurry, and secondary pollution can be caused by improper treatment. With the gradual adoption of the dry manure cleaning process in large-scale farms in China, the yield of solid manure is increased, and the development of dry anaerobic fermentation technology in China is promoted. But the dry fermentation material has high solid content, and the problems of slow degradation rate of the substrate, low mass and heat transfer efficiency and the like exist, so that the utilization rate of the fermentation residues is low. Anaerobic fermentation usually shows a good gas production effect under medium-high temperature conditions, so additional heat preservation measures are needed, and the energy consumption is high. The aerobic fermentation can utilize the residues generated by the anaerobic fermentation to carry out composting to produce the fertilizer, but the anaerobic fermentation gas generation and the aerobic fermentation fertilizer production are two mutually independent processes in the aspect of engineering operation, the methane and the organic fertilizer cannot be simultaneously produced, the gas generation and fertilizer production periods are both longer, more equipment is needed, the energy consumption is high, and the continuous operation efficiency of the engineering is influenced.
Disclosure of Invention
The utility model aims at providing a livestock and poultry excrement straw resourceful treatment device to it is discontinuous with the aerobic fermentation production process to solve anaerobic fermentation, and the gas manure production meets an urgent need.
The utility model discloses technical scheme as follows: a livestock and poultry manure straw recycling treatment device comprises a continuous anaerobic dry fermentation device, an aerobic fermentation composting device and a continuous anaerobic wet fermentation device, wherein the continuous anaerobic wet fermentation device comprises a second feeding hole, a second gas storage tank and a liquid storage tank; the inner cavity of the continuous anaerobic dry fermentation device is provided with a spray pipeline, and a liquid storage tank of the continuous anaerobic wet fermentation device is connected with the spray pipeline through a liquid storage pipeline.
Furthermore, a first sealing valve is arranged on a feed inlet of the continuous anaerobic dry fermentation device.
Further, a screw conveyor is arranged in the continuous anaerobic dry fermentation device.
Furthermore, a circulating water bath interlayer is arranged on the inner wall of the continuous anaerobic dry fermentation device and is connected with a constant temperature water bath tank.
The utility model discloses produce gas and aerobic fermentation compost with anaerobic fermentation and combine, realize the gas manure coproduction, not only effectively utilized the anaerobic fermentation residual, can give anaerobic fermentation with the heat transfer that aerobic fermentation produced again, reduce the energy consumption.
The utility model selects crop straws and livestock and poultry manure as fermentation raw materials, and adjusts the mixing proportion of the raw materials so as to satisfy the carbon-nitrogen ratio required by normal gas production. When the device is operated, firstly, continuous anaerobic dry fermentation is carried out to produce biogas, fresh materials are added every day, fermentation residues such as biogas residues and the like are discharged, the discharged fermentation residues directly enter an aerobic fermentation area to carry out aerobic fermentation composting through aeration, and the anaerobic fermentation gas production and the aerobic fermentation composting are carried out simultaneously by utilizing the retention time difference of the continuous anaerobic dry fermentation and the aerobic fermentation. And when 80% of the materials in the aerobic fermentation area are stacked, starting wet anaerobic fermentation outside the aerobic fermentation area, and realizing heat preservation outside the wet anaerobic fermentation by using heat generated by the aerobic fermentation. During the operation of the wet anaerobic fermentation, fresh materials are added every day, fermentation residues such as biogas slurry and the like are discharged, the biogas slurry is collected in a liquid storage tank, and the dry anaerobic fermentation materials are sprayed through a peristaltic pump and a spraying pipeline, so that substances such as small molecular acid, microorganisms and the like are supplemented for the dry anaerobic fermentation materials, the degradation rate of the dry anaerobic fermentation substrate is further improved, and the gas production efficiency is improved.
The utility model is characterized in that:
(1) the fermentation residues generated by the continuous anaerobic dry fermentation are directly subjected to aerobic fermentation composting, so that not only is the production of methane realized, but also the production of organic fertilizer is realized, and the purpose of co-production of gas fertilizer is achieved.
(2) The wet anaerobic fermentation device is arranged outside the aerobic fermentation area, heat generated by aerobic fermentation can be used for heat preservation, an additional heat preservation device is not needed, and energy consumption is reduced.
(3) The biogas slurry generated by the wet anaerobic fermentation is used for spraying dry anaerobic fermentation materials, so that the dry anaerobic fermentation materials are supplemented with substances such as micromolecular acid, microorganisms and the like, and the gas generation efficiency of the dry anaerobic fermentation is further improved.
Drawings
FIG. 1 is a device for recycling livestock and poultry manure and straws.
The reference numerals have the following meanings: 1-continuous anaerobic dry fermentation device, 2-aerobic fermentation composting device, 3-continuous anaerobic wet fermentation device, 101-first feed inlet, 102-first sealing valve, 103-screw conveyer, 104-spray pipeline, 105-circulating water bath interlayer, 106-shelf, 107-constant temperature water bath box, 108-first gas storage tank, 109-first gas storage valve, 110-discharge port, 201-aeration pipeline, 202-aerobic fermentation valve, 203-fan, 301-second feed inlet, 302-second sealing valve, 303-second gas storage tank, 304-second gas storage valve, 305-liquid storage valve, 306-liquid storage tank, 307-peristaltic pump and 308-liquid storage pipeline.
Detailed Description
The specific structure and operation of the present invention will be further described with reference to the accompanying drawings.
The working principle is as follows: a livestock and poultry manure straw recycling treatment device mainly comprises a continuous anaerobic dry fermentation device, an aerobic fermentation composting device and a continuous anaerobic wet fermentation device. Firstly, continuous anaerobic dry fermentation is carried out, fresh materials are added into a reaction device every day, the fermented materials are conveyed to an outlet of the reaction device through a screw conveyor, and then the fermented materials enter an aerobic fermentation area through a pipeline. When the continuous anaerobic dry fermentation device runs, the fermentation temperature is kept at the medium temperature or the high temperature through the constant-temperature hot water bath interlayer, and the generated gas is collected in the gas storage tank through the gas collection pipeline. And after the fermentation residues enter the aerobic fermentation zone, opening a fan, and aerating the materials in the zone through an aeration pipeline. When the material in the aerobic fermentation zone is piled to 80%, starting the continuous anaerobic wet fermentation device, feeding fresh materials to the reaction device every day, collecting biogas slurry discharged every day in a liquid storage tank, and spraying the dry anaerobic fermentation material through a peristaltic pump and a spraying pipeline. The temperature required by the continuous anaerobic wet fermentation device during operation comes from heat generated by aerobic fermentation, an additional heat preservation device is not required to be added, and the generated gas is collected in the gas storage tank through the gas collection pipeline.
The continuous anaerobic dry fermentation device 1 comprises a first feeding hole 101, a discharging hole 110 and a first gas storage tank 108, wherein a first gas storage valve 109 is arranged on a connecting pipeline of the first gas storage tank 108.
An aeration pipeline 201 is arranged in the aerobic fermentation device 2, the aeration pipeline 201 is connected with a fan 203 and the fan 203, and an aerobic fermentation valve 202 is arranged at the inlet of the aeration pipeline 201.
The top of the continuous anaerobic wet fermentation device 3 is connected with a second gas storage tank 303, the bottom of the continuous anaerobic wet fermentation device 3 is connected with a liquid storage tank 306, and a peristaltic pump 307 is arranged on a liquid storage pipeline 308. A second sealing valve 302 is arranged on a connecting pipeline of a second feeding hole 301 of the continuous anaerobic wet fermentation device 3, a second gas storage valve 304 is arranged on a connecting pipeline of a second gas storage tank 303, and a liquid storage valve 305 is arranged on a connecting pipeline of a liquid storage tank 306.
When the continuous anaerobic dry fermentation device 1 is used, the continuous anaerobic dry fermentation device 1 is placed on the frame 106, when the device is operated, materials are put into the first feeding hole 101, the first sealing valve 102 is manually rotated to seal the reaction area, the screw conveyor 103 is started, the conveyed materials move towards the discharging hole 110, and the materials near the discharging hole are pushed to enter the aerobic fermentation area. The fermentation temperature is kept at a medium temperature (38-42 ℃) throughout the anaerobic fermentation period by means of a constant temperature water bath 107 and a circulating hot water bath sandwich 105. During anaerobic fermentation, the first gas storage valve 109 is opened, and the generated biogas enters the first gas storage tank 108 through the gas collection pipeline. After the wet anaerobic fermentation is started, the biogas slurry is sprayed to the materials in the continuous anaerobic dry fermentation device through the spraying pipeline 104. The spraying amount/material quality is controlled to be 0.2-0.5, and the spraying frequency is controlled to be 3-6 times/day.
During aerobic fermentation, the aerobic fermentation valve 202 is opened, materials in the aerobic fermentation zone are aerated through the fan 203 and the aeration pipeline 201, the aeration amount is controlled to be 0-50L/min, and the aeration frequency is controlled to be 2-8 times/day.
When the continuous anaerobic wet fermentation device operates, materials are put into the second feeding hole 301, the reaction area is sealed by manually rotating the second sealing valve 302, the liquid storage valve 305 is opened when biogas slurry is discharged, the biogas slurry is collected in the liquid storage tank 306, and the biogas slurry is conveyed to the continuous anaerobic fermentation spraying pipeline through the peristaltic pump 307. During anaerobic fermentation, the second gas storage valve 304 is opened, and the generated biogas enters the second gas storage tank 303 through the gas collection pipeline.
Claims (4)
1. The utility model provides a beasts and birds excrement and sewage straw resourceful treatment device, includes dry fermenting installation of continuous anaerobism (1), aerobic fermentation composting device (2), wet fermenting installation of continuous anaerobism (3) include second feed inlet (301), second gas holder (303), liquid storage pot (306), its characterized in that: a discharge port (110) of the continuous anaerobic dry fermentation device (1) is connected with the aerobic fermentation composting device (2), and the continuous anaerobic wet fermentation device (3) is arranged outside the aerobic fermentation composting device (2); the inner cavity of the continuous anaerobic dry fermentation device (1) is provided with a spray pipeline (104), and a liquid storage tank (306) of the continuous anaerobic wet fermentation device (3) is connected with the spray pipeline (104) through a liquid storage pipeline (308).
2. The livestock and poultry manure straw recycling treatment device according to claim 1, which is characterized in that: a first sealing valve (102) is arranged on a feeding hole (101) of the continuous anaerobic dry fermentation device.
3. The livestock and poultry manure straw recycling treatment device according to claim 1, which is characterized in that: the inside of the continuous anaerobic dry fermentation device is provided with a screw conveyor (103).
4. The livestock and poultry manure straw recycling treatment device according to claim 1, which is characterized in that: the inner wall of the continuous anaerobic dry fermentation device (1) is provided with a circulating water bath interlayer (105), and the circulating water bath interlayer (105) is connected with a constant temperature water bath tank (107).
Priority Applications (1)
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CN202120718392.0U CN214881023U (en) | 2021-04-09 | 2021-04-09 | Livestock and poultry manure straw resourceful treatment device |
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CN202120718392.0U CN214881023U (en) | 2021-04-09 | 2021-04-09 | Livestock and poultry manure straw resourceful treatment device |
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CN202120718392.0U Active CN214881023U (en) | 2021-04-09 | 2021-04-09 | Livestock and poultry manure straw resourceful treatment device |
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2021
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