CN108661365A - The utilization system of livestock and poultry cultivation and agricultural greenhouse - Google Patents
The utilization system of livestock and poultry cultivation and agricultural greenhouse Download PDFInfo
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- CN108661365A CN108661365A CN201710207974.0A CN201710207974A CN108661365A CN 108661365 A CN108661365 A CN 108661365A CN 201710207974 A CN201710207974 A CN 201710207974A CN 108661365 A CN108661365 A CN 108661365A
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- 244000144977 poultry Species 0.000 title claims abstract description 66
- 244000144972 livestock Species 0.000 title claims abstract description 65
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 204
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 172
- 238000000855 fermentation Methods 0.000 claims abstract description 69
- 230000004151 fermentation Effects 0.000 claims abstract description 66
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000001257 hydrogen Substances 0.000 claims abstract description 51
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 51
- 238000004519 manufacturing process Methods 0.000 claims abstract description 46
- 239000010865 sewage Substances 0.000 claims abstract description 44
- 239000010828 animal waste Substances 0.000 claims abstract description 35
- GBMDVOWEEQVZKZ-UHFFFAOYSA-N methanol;hydrate Chemical compound O.OC GBMDVOWEEQVZKZ-UHFFFAOYSA-N 0.000 claims abstract description 32
- 230000001105 regulatory effect Effects 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 210000003608 fece Anatomy 0.000 claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- 238000000605 extraction Methods 0.000 claims abstract description 9
- 230000002194 synthesizing effect Effects 0.000 claims abstract description 9
- 238000011010 flushing procedure Methods 0.000 claims abstract description 7
- 210000002700 urine Anatomy 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 39
- 239000007789 gas Substances 0.000 claims description 26
- 239000002002 slurry Substances 0.000 claims description 26
- 238000010438 heat treatment Methods 0.000 claims description 19
- 239000003895 organic fertilizer Substances 0.000 claims description 19
- 239000000446 fuel Substances 0.000 claims description 15
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 14
- 239000012528 membrane Substances 0.000 claims description 13
- 238000009423 ventilation Methods 0.000 claims description 12
- 238000012545 processing Methods 0.000 claims description 11
- 239000007921 spray Substances 0.000 claims description 11
- 239000007864 aqueous solution Substances 0.000 claims description 9
- 230000005611 electricity Effects 0.000 claims description 9
- 239000007858 starting material Substances 0.000 claims description 8
- 229910021529 ammonia Inorganic materials 0.000 claims description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000003337 fertilizer Substances 0.000 claims description 5
- 239000011229 interlayer Substances 0.000 claims description 5
- 238000003786 synthesis reaction Methods 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 3
- 230000002550 fecal effect Effects 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 238000000889 atomisation Methods 0.000 claims 1
- 239000010410 layer Substances 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- 238000010521 absorption reaction Methods 0.000 description 7
- 238000000926 separation method Methods 0.000 description 7
- 239000001569 carbon dioxide Substances 0.000 description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 239000002028 Biomass Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04H—BUILDINGS OR LIKE STRUCTURES FOR PARTICULAR PURPOSES; SWIMMING OR SPLASH BATHS OR POOLS; MASTS; FENCING; TENTS OR CANOPIES, IN GENERAL
- E04H5/00—Buildings or groups of buildings for industrial or agricultural purposes
- E04H5/08—Buildings or groups of buildings for agricultural purposes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Architecture (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Treatment Of Sludge (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to cultivation and technical field of resource comprehensive utilization, more particularly to the utilization system of livestock and poultry cultivation and agricultural greenhouse, it includes livestock and poultry farm, the animal waste thermo-power station and agricultural greenhouse on livestock and poultry farm periphery is arranged, collecting dung pond of the setting for storing feces of livestock and poultry and the sewage collecting pool for storing the sewage such as livestock and poultry urine and flushing water in livestock and poultry farm；The warm and humid regulating device for adjusting canopy temperature and humidity is provided in agricultural greenhouse；The animal waste thermo-power station include sewage marsh gas fermentation pool, excrement marsh gas fermentation pool, the methane extraction element for biogas to be isolated to methane, for by the methanol synthesizer of methane synthesizing methanol, methanol-water hydrogen manufacturing reformer and control device.The animal waste thermo-power station of the present invention realizes the Efficient Conversion of thermal energy and electric energy using animal waste on the spot, and is system power itself heat supply, realizes the comprehensive utilization of the energy.
Description
Technical field
The present invention relates to cultivation and technical field of resource comprehensive utilization, and in particular to the synthesis of livestock and poultry cultivation and agricultural greenhouse
Utilize system.
Background technology
Environmental pollution and energy shortage are global two principal themes, develop environmental improvement and the regenerative resource life of green
The technology of production is extremely urgent.According to statistics, the animal waste that China's scale animal and poultry cultivation generates every year（Excrement）It reaches
To about 3,800,000,000 tons, if being fully converted into biogas is equivalent to 1.62 hundred million tons of standard coals, and wherein only has about 15% and be equipped with biogas engineering
Processing equipment.Feces of livestock and poultry has become one of major source of agricultural non-point source pollution, and a large amount of feces of livestock and poultry is unprocessed, without authorization
Discharge, serious to polluted living environment and underground water source, waste, the pollution of foul smell are sustainable to agricultural, the health of aquaculture
Development causes grave danger.However, animal waste can both become pollution sources, it is also possible to become good biomass energy.
In the prior art, biomass producing methane has been popularized for many years.In order to efficiently use the animal dung generated in livestock and poultry cultivation
Just, some areas start with feces of livestock and poultry manufacture biogas.Biogas be organic substance under anaerobic, by the hair of microorganism
Ferment acts on and a kind of fuel gas of generation.But the method that excrement is handled during existing livestock and poultry cultivation, it is existing main
Problem is：（1）The treatment effeciency of feces of livestock and poultry is low at present, and without integrated treatment, and equipment relies primarily on the height in external power station
Pressure centralization power generation is powered, and can not be the remote districts power supply having inconvenient traffic, to limit the selection of farming site；
（2）Also have in the prior art and generated electricity using biogas, but existing methane power generating system be by way of biogas combustion into
Row heat energy power-generating is first converted into mechanical energy from thermal energy, then is converted into electric energy from mechanical energy, secondary conversion efficiency is too low, therefore not
It can be used widely；（3）The prior art prepares the biogas residue after biogas using feces of livestock and poultry anaerobic fermentation and biogas slurry directly fills
And discharge, it not only pollutes the environment, but also waste resource, since biogas slurry and biogas residue contain abundant nutriment, warp
It can be converted into high-efficiency organic fertilizer after processing and processing.
Invention content
For the prior art, there are above-mentioned technical problems, and the purpose of the present invention is to provide a kind of livestock and poultry cultivation and agricultural are big
The utilization system of canopy, the system realize thermal energy and electricity on the spot using a large amount of animal wastes that livestock and poultry farm generates
Can Efficient Conversion, and carry out the regulating temperature and humidity of agricultural greenhouse using the thermal energy and electric energy and be system power itself heat supply,
Realize the comprehensive utilization of the energy.
To achieve the above object, the present invention provides following technical scheme：
The utilization system of livestock and poultry cultivation and agricultural greenhouse, including livestock and poultry farm, setting are provided on livestock and poultry farm periphery
Animal waste thermo-power station and agricultural greenhouse, in livestock and poultry farm collecting dung pond of the setting for storing feces of livestock and poultry and
Sewage collecting pool for storing the sewage such as livestock and poultry urine and flushing water；It is provided in agricultural greenhouse for adjusting canopy temperature
With the warm and humid regulating device of humidity；The animal waste thermo-power station includes sewage marsh gas fermentation pool, excrement marsh gas fermentation pool, uses
In biogas is isolated to the methane extraction element of methane, for by the methanol synthesizer of methane synthesizing methanol, methanol-water hydrogen manufacturing
Reformer, fuel cell and control device, the methanol-water hydrogen manufacturing reformer are provided with for needed for the reaction of methanol-water reformation hydrogen production
The electric heater of temperature, the control device include controller and the power output end mouth for exporting electric energy outward, wherein：
The excrement of collection is delivered to excrement marsh gas fermentation pool by the collecting dung pond, and the sewage collecting pool passes through pipeline and institute
State the connection of sewage marsh gas fermentation pool, the sewage marsh gas fermentation pool and fecal pollution just marsh gas fermentation pool methane outlet successively with methane
Extraction element, methanol synthesizer connection, the connection of methanol-water hydrogen manufacturing reformer；The methanol prepared by the methanol synthesizer with
The mixed solution of water is delivered to the reformation hydrogen production reaction that first alcohol and water occurs in the methanol-water hydrogen manufacturing reformer by delivery pump,
Hydrogen is made and high temperature residual air, the hydrogen are delivered to fuel cell and produce electricl energy, which is institute by power output end mouth
State other power supply for electrical equipment in delivery pump, electric heater, warm and humid regulating device and system；The high temperature residual air is collected supreme
Warm residual air collection device for biogas fermentation, organic fertilizer fermentation and methanol synthesis reaction in system and warm and humid regulating device into
Temperature needed for the warm and humid adjusting of row.
Wherein, the warm and humid regulating device includes mixed ventilation device, the wind turbine for injecting outside air and for injecting
Steam and the atomizer for connecting water source, the air inlet of the mixed ventilation device respectively by pipeline and high temperature residual air collection device,
Wind turbine is connected with atomizer, and the mixed ventilation device is provided with mixed air cavity, is equipped in the mixed air cavity for making wind turbine convey
What the steam three of air, the high temperature residual air of high temperature residual air collection device conveying and atomizer conveying was uniformly mixed snakelike homogenizes
Channel.
Wherein, the air inlet for stating mixed ventilation device is connect by the first heating pipeline with the high temperature residual air collection device,
The first heating pipeline is provided with the regulating valve being connect with controller, is provided in the agricultural greenhouse and is connect with controller
Temperature sensor and humidity sensor, the wind turbine and atomizer are electrically connected with the controller respectively.
Wherein, further include biogas slurry and biogas residue processing unit, the biogas slurry and biogas residue processing unit includes buffer pool, is separated by solid-liquid separation
The discharge port of device, biogas slurry pond, biogas residue pond and membrane filter, the excrement marsh gas fermentation pool passes through buffer pool and the separation of solid and liquid
Device connects, the biogas slurry outlet of the solid-liquid separator and the sewage marsh gas fermentation pool successively with the biogas slurry pond, membrane filtration
Device connects, and the biogas residue outlet of the solid-liquid separator is connected to the biogas residue pond.
Wherein, the livestock and poultry farm is provided with flusher, and the purified liquor outlet of the membrane filter connects the flushing
Device.
Wherein, further include organic fertilizer manufacturing device, the organic fertilizer manufacturing device includes enrichment facility and organic fertilizer storage
The dope outlet of device, the membrane filter is connect with the enrichment facility, organic fertilizer memory successively.
Wherein, be provided with spray equipment in the agricultural greenhouse, the mouth spray of the spray equipment by pipeline with it is described
The discharge port of organic fertilizer memory connects.
Wherein, the pool wall and/or bottom of pond of the sewage marsh gas fermentation pool and excrement marsh gas fermentation pool are provided with for being passed through
The interlayer of heat medium, the air inlet of the interlayer heat pipeline by described second and connect with the high temperature residual air collection device
It connects, the second heating pipeline is provided with the regulating valve being connect with controller, the sewage marsh gas fermentation pool and excrement biogas hair
The temperature sensor being connect with controller is provided in ferment pond.
Wherein, the methanol synthesizer includes sequentially connected compressor, methyl alcohol synthetic reactor, gas-liquid separator and methanol
Aqueous solution memory, by the ammonia absorption tower gas outlet export methane gas and oxygen respectively by conveyance conduit with
The air inlet of compressor is connected to, and the liquid outlet of the gas-liquid separator is connect with the methanol aqueous solution memory, the gas-liquid
The gas outlet of separator is connected to by circulation line with the air inlet of compressor；The conveyance conduit and circulation line are both provided with
The gas flow control valve being connect with controller, the methyl alcohol synthetic reactor, which is provided with, to be connect with the high temperature residual air collection device
Third heats pipeline, and third heating pipeline is provided with regulating valve connect with controller, be provided in methyl alcohol synthetic reactor and
The temperature sensor and pressure sensor of controller connection.
Wherein, the methanol-water hydrogen manufacturing reformer is provided with starter, and the starter is reformed in methanol-water hydrogen manufacturing
It is the electric heater and delivery pump power supply in device start-up course.
Beneficial effects of the present invention：
The livestock and poultry cultivation of invention and the utilization system of agricultural greenhouse, including livestock and poultry farm, setting are in livestock and poultry farm week
The animal waste thermo-power station and agricultural greenhouse on side, animal waste thermo-power station are generated a large amount of using neighbouring livestock and poultry farm
Animal waste（Include mainly excrement and sewage two parts）, biogas fermentation is carried out, the biogas of generation first passes through methane and carries
Device is taken to extract methane, then methane is through methanol synthesizer synthesizing methanol, and the mixed solution of the methanol and water is as methanol
The raw material of water reformation hydrogen production reaction, is made hydrogen and high temperature residual air, hydrogen therein are delivered to fuel cell and produce electricl energy again, should
Electric energy is all power supply for electrical equipment of livestock and poultry farm, agricultural greenhouse and animal waste thermo-power station, more than high temperature therein
The temperature of gas is up to 300 ~ 600 DEG C, and the thermal energy of this part high-quality is biogas fermentation in animal waste thermo-power station, methane synthesis
Methanol, which reacts, and agricultural greenhouse is warm and humid adjusts the thermal energy needed for providing.Compared with prior art, animal waste of the invention
Thermo-power station passes through the realization electricity of animal waste-biogas-methanol-electric energy/thermal energy using animal waste as raw material
Energy, the Efficient Conversion of thermal energy and utilization, the electric energy which generates directly are periphery livestock and poultry farm and agriculture
Sparetime university's canopy power supply, reaches self-sufficiency, and is not necessarily to external power supply, and the electric energy of the system output is direct current, is without conversion
It can directly use for DC electric apparatus, compared to the mode that current high direct voltage centralization generates electricity, have with with sending out, be easy to be distributed
Installation, feature at low cost, are not limited, which is more suitable for rural culture industry by traffic, place；Separately
On the one hand, the thermal energy of a large amount of high-quality produced by being reacted in methanol-water reformation hydrogen production using animal waste thermo-power station（More than high temperature
The temperature of gas is up to 300 ~ 600 DEG C）, this partial heat energy is fully utilized, be directly biogas fermentation, methane synthesizing methanol it is anti-
It answers and warm and humid adjust of agricultural greenhouse provides required thermal energy.The present invention can be according to needed for animal waste thermo-power station as a result,
The dosage of animal waste, the amount for being converted into methanol, the temperature needed for each heating module, each electricity consumption module power and
The electric energy of the thermal energy and fuel cell output that are generated in the reaction of methanol-water reformation hydrogen production carries out energy perseverance calculation, to support livestock and poultry
It grows waste to be associated with thermal energy, electric energy, forms automation control, energy-saving and environmental protection, the recyclable ecosystem, make biomass energy
Source is comprehensively utilized, with wide commercial application foreground.
Description of the drawings
Fig. 1 is the structural schematic diagram of the livestock and poultry cultivation of the present invention and the utilization system of agricultural greenhouse.
Fig. 2 is the structural representation of the methanol synthesizer of the livestock and poultry cultivation of the present invention and the utilization system of agricultural greenhouse
Figure.
Reference numeral：
Fowl farm 1, collecting dung pond 11, sewage collecting pool 12, flusher 13；
Animal waste thermo-power station 2, sewage marsh gas fermentation pool 21, excrement marsh gas fermentation pool 22, methane extraction element 23；
Methanol synthesizer 24, compressor 241, methyl alcohol synthetic reactor 242, gas-liquid separator 243, methanol aqueous solution memory 244；
Methanol-water hydrogen manufacturing reformer 25, fuel cell 26, electric heater 27, control device 28, delivery pump 29；
Agricultural greenhouse 3, spray equipment 31；
Warm and humid regulating device 4, snakelike homogenizes channel 411, wind turbine 42, atomizer 43 at mixed ventilation device 41；
High temperature residual air collection device 5；
Biogas slurry and biogas residue processing unit 6, buffer pool 61, solid-liquid separator 62, biogas slurry pond 63, biogas residue pond 64, membrane filter 65；
Liquid concentration fertilizer processing unit (plant) 7, enrichment facility 71, organic fertilizer memory 72；
Heat exchanger 8；
First heating pipeline 10, second heats pipeline 20, third heating pipeline 30, circulation line 40, regulating valve 50, gas flow
Control valve 60.
Specific implementation mode
Below in conjunction with specific embodiment and attached drawing, the present invention is described in detail.
The utilization system of livestock and poultry cultivation and agricultural greenhouse, as shown in Figure 1, including livestock and poultry farm 1, being arranged in livestock and poultry
The animal waste thermo-power station 2 and agricultural greenhouse 3 on farm periphery, livestock and poultry farm 1 is interior to be arranged for storing feces of livestock and poultry
Collecting dung pond collecting dung pond 11 and detention tank sewage collecting for storing the sewage such as livestock and poultry urine and flushing water
Pond 12；The warm and humid regulating device 4 for adjusting canopy temperature and humidity is provided in agricultural greenhouse 3；The animal waste
Thermo-power station 2 includes sewage marsh gas fermentation pool 21, excrement marsh gas fermentation pool 22, extracts dress for biogas to be isolated to the methane of methane
Set 23, for filling the methanol synthesizer 24 of methane synthesizing methanol, methanol-water hydrogen manufacturing reformer 25, fuel cell 28 and control
28 are set, methanol-water hydrogen manufacturing reformer 25 is provided with the electric heater 27 that required temperature is reacted for methanol-water reformation hydrogen production, control dress
It sets including controller and the power output end mouth for exporting electric energy outward, wherein：
A large amount of animal wastes that farm's livestock and poultry cultivation process generates include excrement and sewage（Mainly livestock and poultry urine and
Flushing water）It is delivered to collecting dung pond 11 after the unified collection of two parts, wherein excrement, the sewage such as livestock and poultry urine and flushing water can lead to
Piping is delivered to sewage collecting pool 12, and collecting dung pond 11 is connected to by high-pressure pump with excrement marsh gas fermentation pool 22, sewage natural pond
The methane outlet of gas fermentation vat 21 and excrement marsh gas fermentation pool 22 is filled with methane extraction element 23, methanol-fueled CLC successively by pipeline
24 connections are set, the liquid outlet of methanol synthesizer 24 is connect by delivery pump 29 with methanol-water hydrogen manufacturing reformer 25.During being somebody's turn to do
Sewage clear liquid after 12 precipitation process of sewage collecting pool enters sewage marsh gas fermentation pool 21 and carries out biogas fermentation, and sewage collecting
The dope of 12 bottom of pond enters excrement marsh gas fermentation pool 22 together with the excrement in collecting dung pond 11 and carries out biogas fermentation, due to excrement
Just different with the main component of sewage, water content, the two is separated into carry out anaerobic fermentation, the yield of biogas can be improved.Sewage
The biogas that marsh gas fermentation pool 21 and excrement marsh gas fermentation pool 22 generate first passes through methane extraction element 23 and extracts methane, then obtains
The methane obtained enters back into 24 synthesizing methanol of methanol synthesizer.
What the mixed liquor of the above-mentioned first alcohol and water prepared by methanol synthesizer 24 was reacted as methanol-water reformation hydrogen production again
The reformation hydrogen production reaction of first alcohol and water occurs under conditions of in methanol-water hydrogen manufacturing reformer 25 in high mild catalyst for raw material
（The reaction of methanol-water reformation hydrogen production is the prior art, is no longer described in detail in the present embodiment）, obtained to be with carbon dioxide and hydrogen
Main mixed gas, the mixed gas isolate hydrogen and high temperature residual air through separation chamber, which is delivered to the production of fuel cell 26
Raw electric energy, the electric energy pass through other electrical equipments confession that power output end mouth is in delivery pump 29, electric heater 27 and system
Electricity, delivery pump 29 is electrically connected with the controller, it can be achieved that automation control.The animal waste thermo-power station 2 realizes that livestock and poultry are supported on the spot
Efficient Conversion and the utilization of waste-biogas-methanol-electric energy are grown, it is self-sufficient, it is not necessarily to external power supply.And the livestock and poultry are discarded
The electric energy that object thermo-power station 2 exports is direct current, is directly used for DC electric apparatus, without transformer module and subsequent rectification mould
Block etc. has the characteristics that with with sending out, being easy to distributing installation, more compared to the mode that current high direct voltage centralization generates electricity
It is suitble to rural culture industry..Meanwhile the temperature for the high temperature residual air isolated by the separation chamber of methanol-water hydrogen manufacturing reformer 25 be 300 ~
600 DEG C, high temperature residual air is collected to high temperature residual air collection device 5, the thermal energy of this part high-quality is directly animal waste heat
Biogas fermentation, the reaction of methane synthesizing methanol and warm and humid adjust of agricultural greenhouse provide required temperature in power station, greatly reduce
Energy consumption needed for system conducting self-heating, energy-saving effect are notable.
In the present embodiment, warm and humid regulating device 4 includes mixed ventilation device 41, the wind turbine 42 for injecting outside air and uses
In injection steam and the atomizer 43 at water source is connected, the air inlet of mixed ventilation device 41 passes through pipeline and collected with high temperature residual air respectively
Device 5, wind turbine 42 and atomizer 43 connect, and mixed ventilation device 41 is provided with mixed air cavity, mix in air cavity and are equipped with for making wind turbine 42
The steam three that the high temperature residual air and atomizer 43 that air, the high temperature residual air collection device 5 of conveying convey convey is uniformly mixed
Snakelike homogenize channel 411.When work, animal waste thermo-power station 2 is that agricultural greenhouse 3 conveys electric energy and thermal energy, high temperature
Residual air, outside air and steam are entered mix in air cavity snakelike by pipeline and homogenize channel 411 respectively, are formed and are uniformly mixed and have
There is the mixed steam of certain temperature and humidity, then be delivered in agricultural greenhouse 3, to meet the temperature in greenhouse needed for crop growth
And humidity.The air inlet of mixed ventilation device 41 is connect by the first heating pipeline 10 with high temperature residual air collection device 5, the first heating
Pipeline 10 is provided with the regulating valve 50 being connect with controller, be provided in agricultural greenhouse the temperature sensor being connect with controller and
Humidity sensor, wind turbine 42 and atomizer 43 are electrically connected with the controller respectively.Warm and humid regulating device 4 passes through regulating valve 50, temperature
Sensor and humidity sensor realize that the automation of temperature and humidity in agricultural greenhouse 3 accurately controls.
In the present embodiment, the utilization system of livestock and poultry cultivation and agricultural greenhouse 3 further include biogas slurry and biogas residue processing unit 6 and
Organic fertilizer manufacturing device 7 for the biogas slurry and biogas residue progress resource reutilization to being generated after biogas fermentation, and is discarded by livestock and poultry
The power supply heat supply of object thermo-power station, realizes its work.Specifically, biogas slurry and biogas residue processing unit 6 includes buffer pool 61, solid-liquid separator
62, the discharge port of biogas slurry pond 63, biogas residue pond 64 and membrane filter 65, excrement marsh gas fermentation pool 22 passes through buffer pool 61 and solid-liquid point
Connected from device 62, the biogas slurry outlet of solid-liquid separator 62 and sewage marsh gas fermentation pool 21 successively with biogas slurry pond 63, membrane filter
The biogas residue outlet of 65 connections, solid-liquid separator 62 is connected to biogas residue pond 64.Organic fertilizer manufacturing device 7 includes enrichment facility 71 and has
The dope outlet of machine fertilizer memory 72, membrane filter 65 is connect with enrichment facility 71, organic fertilizer memory 72 successively.Further,
Livestock and poultry farm 1 is provided with flusher 13, and the purified liquor outlet of membrane filter 65 connects flusher 13.It is set in agricultural greenhouse 3
It is equipped with spray equipment 31, the mouth spray of spray equipment 31 is connect by pipeline with the discharge port of organic fertilizer memory 72.Its work
Principle：Sewage marsh gas fermentation pool 21 mainly carries out biogas fermentation to sewage, and resultant product is mainly biogas slurry after fermentation, by this portion
Point biogas slurry is stored in biogas slurry pond 63.And excrement marsh gas fermentation pool 22 is mainly the biogas fermentation of excrement, and a large amount of natural ponds are generated after fermentation
Slag and a small amount of biogas slurry need to first pass through solid-liquid separator 62 and isolate biogas residue and be stored in the natural pond that biogas residue pond 64 is spare, isolates
Liquid is stored in biogas slurry pond 63.Then, the biogas slurry collected in above-mentioned biogas slurry pond 63 first pass through obtained after membrane filter 65 filters it is clear
Liquid reuse is to flusher 13, as the rinse water of livestock and poultry farm 1, the 65 concentrated device of filtered dope of membrane filter
Liquid concentration fertilizer is obtained after 71 concentrations, and is stored in organic fertilizer memory 72, which can pass through Pipeline transport to agriculture
The spray equipment 31 of sparetime university's canopy 3 is directly sprayed on crop surface, and the organic fertilizer as agricultural planting uses, and can avoid useization
Fertilizer and environmental protection, promote the ecodevelopment of agricultural.
In the present embodiment, animal waste thermo-power station 2 is that biogas fermentation conveys thermal energy, sewage marsh gas fermentation pool 21 and excrement
The pool wall and/or bottom of pond of marsh gas fermentation pool 22 are provided with the interlayer for being passed through heat medium, and the air inlet of interlayer adds by second
Pipe line 20 is connect with high temperature residual air collection device 5.Using high temperature residual air as heat medium, to 21 He of sewage marsh gas fermentation pool
The heating of excrement marsh gas fermentation pool 22 provides the temperature needed for anaerobic fermentation.Second heating pipeline 20, which is provided with, to be connect with controller
It is provided with the temperature sensor being connect with controller in regulating valve 50, sewage marsh gas fermentation pool 21 and excrement marsh gas fermentation pool 22,
In order to the detection and regulation and control to biogas fermentation temperature.
In the present embodiment, methane extraction element 23 includes sequentially connected solid-liquid separator, desulfurizing tower, carbon dioxide absorption
The methane outlet of tower and ammonia absorption tower, sewage marsh gas fermentation pool 21 and excrement marsh gas fermentation pool 22 respectively with solid-liquid separator
Air inlet is connected to, and the gas outlet of ammonia absorption tower is connected to methanol synthesizer 24.Due to biogas fermentation generate biogas be containing
The mixture for having methane, sulfide and carbon dioxide etc. first passes through solid-liquid separator and removes solid impurity, then in turn through de-
Sulphur tower remove sulfide, by carbon dioxide absorption tower remove carbon dioxide, by ammonia absorption tower remove ammonia after obtain it is pure
Higher methane gas is spent, then is delivered to methanol synthesizer 24 and is used to prepare methanol.
In the present embodiment, as shown in Fig. 2, methanol synthesizer 24 includes sequentially connected compressor 241, methyl alcohol synthetic reactor
242, gas-liquid separator 243 and methanol aqueous solution memory 244, by ammonia absorption tower 54 gas outlet export methane gas with
And oxygen is connected to by conveyance conduit with the air inlet of compressor 241 respectively, the liquid outlet and methanol of gas-liquid separator 243 are water-soluble
Liquid memory 244 connects, and the gas outlet of gas-liquid separator 243 is connected to by circulation line 40 with the air inlet of compressor 241.On
During stating, methane gas and outer oxygen（As oxygen cylinder provides oxygen）Methanol is delivered to after the pressurization of compressor 241 to close
It is reacted at 242 internal oxidition of tower and generates methanol, wherein methane and oxygen presses 8 ~ 9:1 ~ 2 volume ratio mixing, at 150 ~ 220 DEG C and
It under conditions of 80 ~ 125 atmospheric pressure, reacts and methanol is made, reaction equation is：2CH4+O2=2CH3OH.In methyl alcohol synthetic reactor 242
The methanol solution that the residual gases such as the methanol of generation and unreacted methane obtain after 243 condensation separation of gas-liquid separator
It is stored in methanol aqueous solution memory 244, the residual gas after separation is back to 241 air inlet of compressor by circulation line 40 again
Mouthful, enter back into 242 synthesizing methanol of methyl alcohol synthetic reactor.Conveyance conduit and circulation line 40 are both provided with the gas being connect with controller
Flow control valve 60, realizes the automation control of gas flow in each pipeline by gas flow control valve 60, compressor 241 by
The electric energy power supply that animal waste thermo-power station 2 exports.Further, animal waste thermo-power station 2 is methanol synthesis reaction conveying heat
Can, methyl alcohol synthetic reactor 242 is provided with the third heating pipeline 30 being connect with high temperature residual air collection device 5, and third heats pipeline 30
On be provided with regulating valve 50, the temperature sensor and pressure sensor being connect with controller are provided in methyl alcohol synthetic reactor 242, from
And realize the automation control to methyl alcohol synthetic reactor 242 interior reaction temperature and pressure.
In the present embodiment, it is arranged on transfer pipeline between methanol aqueous solution memory 244 and methanol-water hydrogen manufacturing reformer 25
There is heat exchanger 8, the high-temperature hydrogen that the methanol aqueous solution of low temperature and separation chamber 82 isolate is after heat exchanger 8 carries out heat exchange, hydrogen
Enter fuel cell 26 after gas cooling, methanol-water is further heated, and evaporation in methanol-water hydrogen manufacturing reformer 25 is then sent to
Gasification.
In the present embodiment, methanol-water hydrogen manufacturing reformer 25 is provided with starter.First, starter is in methanol-water hydrogen manufacturing
In 25 start-up course of reformer, it is that delivery pump 29 and electric heater 27 are powered, so that the reaction of methanol-water reformation hydrogen production starts, obtains
Hydrogen and high temperature residual air, hydrogen enter fuel cell 26, and the work of fuel cell 26 produces electricl energy, thus animal waste thermo-power station
2 produce electricl energy and thermal energy, then are that whole system is powered heat supply, to form the circulatory system.Specifically, starter is electric power storage
Pond；Or be combustion-type starter, it is heated for reformer chamber 81 by combustion methanol；Or be hydrogen storage bottle, which can
It is 26 inputting hydrogen of fuel cell in 25 start-up course of methanol-water hydrogen manufacturing reformer, the work of fuel cell 26 is made to produce electricl energy,
And then it powers for delivery pump 29 and electric heater 27.
The present invention can according to the dosage of animal waste needed for animal waste thermo-power station 2, be converted into methanol
The thermal energy generated in amount, the temperature needed for each heating module, the power of each electricity consumption module and the reaction of methanol-water reformation hydrogen production with
And the electric energy of fuel cell output carries out energy perseverance calculation, to which animal waste to be associated with thermal energy, electric energy, forms ecology
The circulatory system, with wide commercial application foreground.
Finally it should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention, rather than the present invention is protected
The limitation of range is protected, although being explained in detail to the present invention with reference to preferred embodiment, those skilled in the art answer
Work as understanding, technical scheme of the present invention can be modified or replaced equivalently, without departing from the reality of technical solution of the present invention
Matter and range.
Claims (10)
1. the utilization system of livestock and poultry cultivation and agricultural greenhouse, it is characterised in that：It is supported in livestock and poultry including livestock and poultry farm, setting
The animal waste thermo-power station and agricultural greenhouse on periphery are grown, the excrement for storing feces of livestock and poultry is set in livestock and poultry farm
Collecting pit and sewage collecting pool for storing the sewage such as livestock and poultry urine and flushing water；It is provided in agricultural greenhouse big for adjusting
The warm and humid regulating device of temperature of shed and humidity；The animal waste thermo-power station includes sewage marsh gas fermentation pool, excrement biogas
Fermentation vat, the methane extraction element for biogas to be isolated to methane, for by the methanol synthesizer of methane synthesizing methanol, first
Alcohol water hydrogen manufacturing reformer, fuel cell and control device, the methanol-water hydrogen manufacturing reformer are provided with for methanol-water reformation hydrogen production
The electric heater of required temperature is reacted, the control device includes controller and the power output end for exporting electric energy outward
Mouthful, wherein：
The excrement of collection is delivered to excrement marsh gas fermentation pool by the collecting dung pond, and the sewage collecting pool passes through pipeline and institute
State the connection of sewage marsh gas fermentation pool, the sewage marsh gas fermentation pool and fecal pollution just marsh gas fermentation pool methane outlet successively with methane
Extraction element, methanol synthesizer connection, the connection of methanol-water hydrogen manufacturing reformer；The methanol prepared by the methanol synthesizer with
The mixed solution of water is delivered to the reformation hydrogen production reaction that first alcohol and water occurs in the methanol-water hydrogen manufacturing reformer by delivery pump,
Hydrogen is made and high temperature residual air, the hydrogen are delivered to fuel cell and produce electricl energy, which is institute by power output end mouth
State other power supply for electrical equipment in delivery pump, electric heater, warm and humid regulating device and system；The high temperature residual air is collected supreme
Warm residual air collection device for biogas fermentation, organic fertilizer fermentation and methanol synthesis reaction in system and warm and humid regulating device into
Temperature needed for the warm and humid adjusting of row.
2. the utilization system of livestock and poultry cultivation according to claim 1 and agricultural greenhouse, it is characterised in that：It is described warm and humid
Regulating device includes mixed ventilation device, the wind turbine for injecting outside air and for injecting steam and connecting the atomization at water source
The air inlet of device, the mixed ventilation device is connect by pipeline with high temperature residual air collection device, wind turbine and atomizer respectively, described
Mixed ventilation device is provided with mixed air cavity, and air, high temperature residual air collection device for making wind turbine convey are equipped in the mixed air cavity
What the steam three of high temperature residual air and the atomizer conveying of conveying was uniformly mixed snakelike homogenizes channel.
3. the utilization system of livestock and poultry cultivation according to claim 2 and agricultural greenhouse, it is characterised in that：The mixing
The air inlet of blower is connect by the first heating pipeline with the high temperature residual air collection device, the first heating pipeline setting
There is the regulating valve being connect with controller, the temperature sensor and humidity sensor being connect with controller are provided in the agricultural greenhouse
Device, the wind turbine and atomizer are electrically connected with the controller respectively.
4. the utilization system of livestock and poultry cultivation according to claim 1 and agricultural greenhouse, it is characterised in that：It further include natural pond
Liquid biogas residue processing unit, the biogas slurry and biogas residue processing unit include buffer pool, solid-liquid separator, biogas slurry pond, biogas residue pond and film mistake
The discharge port of filter, the excrement marsh gas fermentation pool is connect by buffer pool with the solid-liquid separator, the solid-liquid separator
It is connect successively with the biogas slurry pond, membrane filter with the outlet of the biogas slurry of the sewage marsh gas fermentation pool, the solid-liquid separator
Biogas residue outlet be connected to the biogas residue pond.
5. the utilization system of livestock and poultry cultivation according to claim 4 and agricultural greenhouse, it is characterised in that：The livestock and poultry
Farm is provided with flusher, and the purified liquor outlet of the membrane filter connects the flusher.
6. the utilization system of livestock and poultry cultivation according to claim 4 and agricultural greenhouse, it is characterised in that：Further include having
Machine fertilizer manufacturing device, the organic fertilizer manufacturing device include enrichment facility and organic fertilizer memory, the dope of the membrane filter
Outlet is connect with the enrichment facility, organic fertilizer memory successively.
7. the utilization system of livestock and poultry cultivation according to claim 6 and agricultural greenhouse, it is characterised in that：The agricultural
Spray equipment is provided in greenhouse, the mouth spray of the spray equipment is connected by the discharge port of pipeline and the organic fertilizer memory
It connects.
8. the utilization system of livestock and poultry cultivation according to claim 1 and agricultural greenhouse, it is characterised in that：The sewage
The pool wall and/or bottom of pond of marsh gas fermentation pool and excrement marsh gas fermentation pool are provided with the interlayer for being passed through heat medium, the folder
The air inlet of layer heats pipeline by described second and is connect with the high temperature residual air collection device, the second heating pipeline setting
There is the regulating valve being connect with controller, is provided in the sewage marsh gas fermentation pool and excrement marsh gas fermentation pool and is connect with controller
Temperature sensor.
9. the utilization system of livestock and poultry cultivation according to claim 1 and agricultural greenhouse, it is characterised in that：The methanol
Synthesizer includes sequentially connected compressor, methyl alcohol synthetic reactor, gas-liquid separator and methanol aqueous solution memory, by the ammonia
The methane gas and oxygen of the gas outlet output of aspiration tower are connected to by conveyance conduit with the air inlet of compressor respectively, institute
The liquid outlet for stating gas-liquid separator is connect with the methanol aqueous solution memory, and the gas outlet of the gas-liquid separator passes through cycle
Pipeline is connected to the air inlet of compressor；The conveyance conduit and circulation line are both provided with the gas flow being connect with controller
Control valve, the methyl alcohol synthetic reactor are provided with the third heating pipeline being connect with the high temperature residual air collection device, the third
Heating pipeline is provided with the regulating valve being connect with controller, and the temperature sensor being connect with controller is provided in methyl alcohol synthetic reactor
And pressure sensor.
10. the utilization system of livestock and poultry cultivation according to claim 1 and agricultural greenhouse, it is characterised in that：The first
Alcohol water hydrogen manufacturing reformer is provided with starter, and the starter is the electricity in methanol-water hydrogen manufacturing reformer start-up course
Heater and delivery pump power supply.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710207974.0A CN108661365A (en) | 2017-03-31 | 2017-03-31 | The utilization system of livestock and poultry cultivation and agricultural greenhouse |
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|---|---|---|---|
| CN201710207974.0A CN108661365A (en) | 2017-03-31 | 2017-03-31 | The utilization system of livestock and poultry cultivation and agricultural greenhouse |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109471476A (en) * | 2019-01-11 | 2019-03-15 | 南安市绿野沼气技术开发研究所 | An energy-saving and environmentally friendly livestock and poultry breeding control system |
| CN116664087A (en) * | 2023-08-02 | 2023-08-29 | 山东赛马力发电设备有限公司 | Comprehensive energy management system |
-
2017
- 2017-03-31 CN CN201710207974.0A patent/CN108661365A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109471476A (en) * | 2019-01-11 | 2019-03-15 | 南安市绿野沼气技术开发研究所 | An energy-saving and environmentally friendly livestock and poultry breeding control system |
| CN116664087A (en) * | 2023-08-02 | 2023-08-29 | 山东赛马力发电设备有限公司 | Comprehensive energy management system |
| CN116664087B (en) * | 2023-08-02 | 2023-10-10 | 山东赛马力发电设备有限公司 | Comprehensive energy management system |
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