CN208485776U - A kind of plug flow type biomass pool solar energy triplet temperature raising device - Google Patents
A kind of plug flow type biomass pool solar energy triplet temperature raising device Download PDFInfo
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- CN208485776U CN208485776U CN201820883734.2U CN201820883734U CN208485776U CN 208485776 U CN208485776 U CN 208485776U CN 201820883734 U CN201820883734 U CN 201820883734U CN 208485776 U CN208485776 U CN 208485776U
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- pond
- sultry
- heliogreenhouse
- sunlight board
- pool
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Abstract
The utility model discloses a kind of plug flow type biomass pool solar energy triplet temperature raising devices, including heliogreenhouse main body, the inside of the heliogreenhouse main body is respectively arranged with the sultry pond of sunlight board and boiler, the middle position of heliogreenhouse body interior is arranged in the boiler, the corner of heliogreenhouse body interior is arranged in the sultry pond of sunlight board, top on the outside of the heliogreenhouse main body is provided with solar thermal collector, the utility model strong innovation, technique is advanced, it is stable, high treating effect, investment cost is low, processing especially suitable for the organic waste of scale livestock farming high concentration, with good economic benefit, social benefit and ecological benefits, a new approach is provided for the processing of livestock and poultry cultivation feces of farm.
Description
Technical field
The utility model belongs to plug flow type biomass pool technical field, and in particular to a kind of plug flow type biomass pool solar energy three
Body temperature raising device.
Background technique
Animal husbandry development is rapid in recent years in China, and the increase of livestock and poultry farms in scale quantity quickly, arrange by livestock and poultry cultivation place
The waste amount put, considerably beyond the bearing capacity of its ambient enviroment.Government wishes the implementation by large and medium-sized biogas project, solution
Certainly pollution of the livestock and poultry farm to ambient enviroment improves the problem of rural energy anxiety nearby.Biogas project plays wherein
Improve environment, production clean energy resource, the important function for developing the high-quality and efficient ecological agriculture.
Existing biogas project by livestock and poultry rinse sewage, manually dry cleaning up excrement enter after being simply mixed anaerobic digestion device into
Row fermentation, such fermentation raw material concentration is unstable (TS2%---15%), and raw material does not enter by heating (normal temperature fermentation)
Installation for fermenting, factor of created gase are low.There are a small number of livestock and poultry farm biogas projects using medium temperature (35 ± 2 DEG C) and hot fermentation (53 ± 2
DEG C), but since Co-generation is not carried out, produced biogas is largely or entirely used for heating for fermentation raw material in low temperature season,
Economic benefit is low, and part biogas project is mounted with large-scale bottle coal multi-fuel fired boiler, makes to keep the temperature to raw material heating and installation for fermenting
It is increased at production cost, negative benefit occurs.Therefore, how to guarantee the long-term stable operation of biogas project, reduce production cost, improve
Economic benefit becomes the key subjects that our biogas scientific research personnel face.
Utility model content
To solve the problems mentioned above in the background art.The utility model provides a kind of plug flow type biomass pool solar energy
Triplet temperature raising device adds with fully giving the raw material into methane-generating pit to heat in advance using heat caused by solar energy
Heat, the characteristics of substantially increasing the utilization rate of renewable energy.
To achieve the above object, the utility model provides the following technical solutions: a kind of plug flow type biomass pool solar energy three
Body temperature raising device, including heliogreenhouse main body, the inside of the heliogreenhouse main body are respectively arranged with the sultry pond of sunlight board and pot
The middle position of heliogreenhouse body interior is arranged in furnace, the boiler, and the sultry pond of sunlight board is arranged in heliogreenhouse master
The corner in internal portion, the top on the outside of the heliogreenhouse main body are provided with solar thermal collector, the sultry pond of sunlight board
Including insulated wall, metering heating bath, channel, water pressure chamber, slag tap between, biogas slurry backflow pool, partition wall, hydrolysis acidification pool, filtration gauze,
Filter column slot, feed(raw material)inlet, wherein the partition wall by the insulated wall from north to south be once divided into the metering heating bath,
The hydrolysis acidification pool and the biogas slurry backflow pool three parts, described one end measured inside heating bath and the biogas slurry backflow pool
It is set as the water pressure chamber, and between the same end inside the hydrolysis acidification pool is set as described and slags tap, the metering heating bath
The partition wall between the hydrolysis acidification pool offers the channel, the hydrolysis acidification close to one end of the water pressure chamber
Pond is provided with the feed(raw material)inlet far from one end between described slag tap, and the filter column slot, institute are fixed on the feed(raw material)inlet
The laid inside for stating filter column slot has the filtration gauze.
As a kind of optimal technical scheme of the utility model, the solar thermal collector passes through pipeline and heat exchange pipe dish
It is connect respectively with the sultry pond of the sunlight board and the boiler.
As a kind of optimal technical scheme of the utility model, the height that the sultry pond of sunlight board is located at north side is
2000mm, and it is 850mm that the sultry pond of the sunlight board, which is located at the height in southern side, angle is 25 degree, the sultry pond of sunlight board
Width be 5000mm, the height of the partition wall is 700mm, and the top frame in the sultry pond of sunlight board is covered with a thickness of 8mm's
Polycarbonate multi-wall sheet.
As a kind of optimal technical scheme of the utility model, a length of 3000mm of the filter column slot, width 1000mm,
With a thickness of 50mm, the net diameter of the filtration gauze is 7mm.
As a kind of optimal technical scheme of the utility model, the polycarbonate multi-wall sheet corresponds to the position of feed(raw material)inlet
It is provided with the removable cover of long 2000mm wide 2000mm.
Compared with prior art, the utility model has the beneficial effects that
1, the utility model largely uses thermal insulation material, heat-absorbing material, heat insulation and transmission material are feed liquid heat preservation, heat, if
Applying required thermal energy is asked for the sun, not only free but also renewable, utilizes solar energy heat collector, heliogreenhouse, sunlight
Plate boils in a covered pot over a slow fire hot pond, heat absorption red-sludge plastic makes full use of solar energy resources in biogas production process, improves methane tank gas production amount；
2, the utility model is suspended solid in raw material and protein, grease, surfactant and Ca+, NH4+, S2- etc.
Substance in decomposing harmful substances (containing disinfected wastewater) stage, is effectively reduced to natural pond by removing excrement slag, sediment, hydrolysis, acidification
The impact and deleterious effects of gas pond aerogenic bacteria, shorten the anaerobism residence time, increase methane-generating pit capacity utilization, avoid simultaneously
Methane-generating pit ensure that the normal work of methane-generating pit installation for fermenting there is a phenomenon where blocking；
3, the utility model adjustment reflux feed liquid makes feed liquid temperature continue to improve, and anaerobic bacteria breeds rapidly, enhances anaerobism
Bacterial activity is conducive to the generation of biogas；
4, the utility model makes raw material cover hydrolysis, acidification, heating and feed liquid reflux automatically certainly using multistage gravity flow technique
Cyclic process, have the characteristics that it is with low investment, without operating cost, convenient for management；
5, the utility model strong innovation, technique is advanced, stable, high treating effect, investment cost are low, particularly suitable
In the processing of the organic waste of scale livestock farming high concentration, there are good economic benefit, social benefit and ecological benefits, for poultry
Fowl cultivation feces of farm processing provides a new approach.
Detailed description of the invention
Attached drawing is used to provide a further understanding of the present invention, and constitutes part of specification, practical with this
Novel embodiment is used to explain the utility model together, does not constitute limitations of the present invention.In the accompanying drawings:
Fig. 1 is the plane figure of the utility model；
Fig. 2 is the structural schematic diagram in the sultry pond of the utility model sunlight board；
Fig. 3 is that the side layout of the utility model schemes；
In figure: 1, heliogreenhouse main body；2, the sultry pond of sunlight board；21, insulated wall；22, heating bath is measured；23, channel；
24, water pressure chamber；25, between slagging tap；26, biogas slurry backflow pool；27, partition wall；28, hydrolysis acidification pool；29, filtration gauze；210, it filters
Column slot；211, feed(raw material)inlet；3, solar thermal collector；4, boiler.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing.In the utility model
Description in, it should be noted that term " center ", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outside"
The orientation or positional relationship of equal instructions is to be based on the orientation or positional relationship shown in the drawings, and being merely for convenience of description, this is practical new
Type and simplified description, rather than the device or element of indication or suggestion meaning must have a particular orientation, with specific orientation
Construction and operation, therefore should not be understood as limiting the present invention.In addition, term " first ", " second ", " third " are only used
In description purpose, it is not understood to indicate or imply and faces ground importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, be also possible to be electrically connected；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
The concrete meaning of language in the present invention.
Embodiment
Fig. 1-3 is please referred to, the utility model is the following technical schemes are provided: a kind of plug flow type biomass pool solar energy triplet increases
Warm equipment, including heliogreenhouse main body 1, the inside of heliogreenhouse main body 1 are respectively arranged with the sultry pond 2 of sunlight board and boiler 4, pot
The middle position inside heliogreenhouse main body 1 is arranged in furnace 4, and turning inside heliogreenhouse main body 1 is arranged in the sultry pond 2 of sunlight board
At angle, the top in 1 outside of heliogreenhouse main body is provided with solar thermal collector 3, and the sultry pond 2 of sunlight board includes insulated wall 21, meter
Amount heating bath 22, channel 23, water pressure chamber 24, slag tap between 25, biogas slurry backflow pool 26, partition wall 27, hydrolysis acidification pool 28, filtration gauze
29, filter column slot 210, feed(raw material)inlet 211, wherein insulated wall 21 is once divided into metering heating bath from north to southern by partition wall 27
22,26 three parts of hydrolysis acidification pool 28 and biogas slurry backflow pool measure one end setting inside heating bath 22 and biogas slurry backflow pool 26
For water pressure chamber 24, and the same end inside hydrolysis acidification pool 28 is set as 25 between slagging tap, and measures heating bath 22 and hydrolysis acidification pool
Partition wall 27 between 28 offers channel 23 close to one end of water pressure chamber 24, and hydrolysis acidification pool 28 is set far between slagging tap 25 one end
It is equipped with feed(raw material)inlet 211, filter column slot 210 is fixed on feed(raw material)inlet 211, the laid inside of filter column slot 210 has filtering yarn
Net 29.
In order to be converted to thermal energy with regulating pondage, supplement cold water, solar radiant energy, pass through pipeline and heat exchange disk
Pipe boils in a covered pot over a slow fire the feed liquid in heat death theory heating bath to sunlight board and carries out quadruple effect heating, biogas is entered after so that feed liquid is reached design temperature
In pond；Winter supplements hot water to methane boiler, and energy saving, further, solar thermal collector 3 passes through pipeline and heat exchange
Pipe dish is connect with the sultry pond 2 of sunlight board and boiler 4 respectively.
For the ease of sunray radiate enter, to greatest extent using solar energy generate heat to pre-treatment feed liquid into
Row second imitates temp.-increasing heating；Simultaneously raw material because guaranteeing sunlight by thermogenetic Odor con trol in the sultry interior of sunlight board
Room air is fresh, and further, the height that the sultry pond 2 of sunlight board is located at north side is 2000mm, and the sultry pond 2 of sunlight board is located at
The height in southern side is 850mm, and angle is 25 degree, and the width in the sultry pond 2 of sunlight board is 5000mm, and the height of partition wall 27 is
700mm, the top frame in the sultry pond 2 of sunlight board are covered with the polycarbonate multi-wall sheet with a thickness of 8mm, and light transmittance is up to 95%, this implementation
The length in the sultry pond 2 of sunlight board is set according to methane-generating pit is long in example.
For the solid content that bulk not readily dissolves in filter stock, keep the solid content entered in pond in raw material small, is easy quilt
Microorganism decomposition, further, a length of 3000mm of filter column slot 210, width 1000mm, with a thickness of 50mm, filtration gauze 29
Net diameter be 7mm.
For the ease of the residue in cleaning filter column slot, further, polycarbonate multi-wall sheet corresponds to feed(raw material)inlet 211
Position is provided with the removable cover of long 2000mm wide 2000mm.
The present embodiment mid-board 27 uses 12 walls, and insulated wall 21 presss from both sides 5 centimeters of thick polystyrene foam plates using 12 walls.
The working principle and process for using of the utility model: the utility model heliogreenhouse main body 1 is methane-generating pit and preceding place
Reason facility is all wrapped in greenhouse, and heliogreenhouse main body 1 gathers heat by greenhouse effects, and indoor minimum temperature generally compares room
Outer temperature is 3~6 degrees Celsius high, high 6~15 degrees Celsius of mean temperature or more, utilizes the greenhouse effects pair in heliogreenhouse main body 1
Sunlight board boils in a covered pot over a slow fire the feed liquid under hot pond and carries out the first effect heating, and boiler 4 supplements hot water to boiler 4 by solar thermal collector 3 when winter,
It recycles a small amount of biological energy source to heat up to boiler 4, through pipeline and heat exchanger coil, is heated to metering 22 feed liquid of heating bath,
Enter in methane-generating pit after so that feed liquid is reached design temperature, hydrolysis acidification pool 28 and 26 pond interior walls of biogas slurry backflow pool and bottom are covered with
Red-sludge plastic covers skin, and red-sludge plastic is corrosion-resistant, anti-aging, and close property is good, and heat absorption capacity is excellent, makes full use of solar energy for feed liquid progress
Third effect heats, and improves feed liquid fermentation temperature, feed liquid discomposing effect is good, and raw material is in 28 pond of hydrolysis acidification pool with gradient hydraulic current
Simultaneously hydrolysis acidification is dropped down, flows automatically through channel 23 and is heated into metering heating bath 22, the raw material to come from hydrolysis acidification pool 28, warp
It crosses after hydrolyzate and becomes the solable matter of microbial digestion, then further decompose, become acetic acid, hydrogen, carbon dioxide etc.
Aerogenic bacteria likes that the substance of " eating ", raw material are heated in metering heating bath 22, enters fermentation in methane-generating pit after reaching design temperature.
Finally, it should be noted that the above descriptions are merely preferred embodiments of the present invention, it is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it is still possible to modify the technical solutions described in the foregoing embodiments, or to part of technical characteristic
It is equivalently replaced.Within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on,
It should be included within the scope of protection of this utility model.
Claims (5)
1. a kind of plug flow type biomass pool solar energy triplet temperature raising device, including heliogreenhouse main body (1), it is characterised in that: institute
The inside for stating heliogreenhouse main body (1) is respectively arranged with the sultry pond of sunlight board (2) and boiler (4), and the boiler (4) was arranged in day
The internal middle position of light greenhouse body (1), the sultry pond of sunlight board (2) setting the turning in heliogreenhouse main body (1) inside
At angle, the top on the outside of the heliogreenhouse main body (1) is provided with solar thermal collector (3), the sultry pond of sunlight board (2) packet
Include insulated wall (21), metering heating bath (22), channel (23), water pressure chamber (24), slag tap between (25), biogas slurry backflow pool (26), every
Wall (27), hydrolysis acidification pool (28), filtration gauze (29), filter column slot (210), feed(raw material)inlet (211), wherein the partition wall
(27) by the insulated wall (21) from north to south be once divided into the metering heating bath (22), the hydrolysis acidification pool (28) and
One end setting of biogas slurry backflow pool (26) three parts, metering heating bath (22) and the biogas slurry backflow pool (26) inside
For the water pressure chamber (24), and the internal the same end of the hydrolysis acidification pool (28) be set as described and slag tap between (25), the meter
The partition wall (27) between amount heating bath (22) and the hydrolysis acidification pool (28) is opened close to the one end of the water pressure chamber (24)
Equipped with the channel (23), the hydrolysis acidification pool (28) is provided with the feed(raw material)inlet far from the one end of (25) between described slag tap
(211), the filter column slot (210), the laid inside of the filter column slot (210) are fixed on the feed(raw material)inlet (211)
There are the filtration gauze (29).
2. a kind of plug flow type biomass pool solar energy triplet temperature raising device according to claim 1, it is characterised in that: described
Solar thermal collector (3) is connected with the sultry pond of the sunlight board (2) and the boiler (4) respectively by pipeline and heat exchange pipe dish
It connects.
3. a kind of plug flow type biomass pool solar energy triplet temperature raising device according to claim 1, it is characterised in that: described
The height that the sultry pond of sunlight board (2) is located at north side is 2000mm, and the sultry pond of the sunlight board (2) is located at the height in southern side and is
850mm, angle are 25 degree, and the width of the sultry pond of sunlight board (2) is 5000mm, and the height of the partition wall (27) is
The top frame of 700mm, the sultry pond of sunlight board (2) are covered with the polycarbonate multi-wall sheet with a thickness of 8mm.
4. a kind of plug flow type biomass pool solar energy triplet temperature raising device according to claim 1, it is characterised in that: described
A length of 3000mm of filter column slot (210), width 1000mm, with a thickness of 50mm, the net diameter of the filtration gauze (29) is 7mm.
5. a kind of plug flow type biomass pool solar energy triplet temperature raising device according to claim 3, it is characterised in that: described
The position that polycarbonate multi-wall sheet corresponds to feed(raw material)inlet (211) is provided with the removable cover of long 2000mm wide 2000mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820883734.2U CN208485776U (en) | 2018-06-07 | 2018-06-07 | A kind of plug flow type biomass pool solar energy triplet temperature raising device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820883734.2U CN208485776U (en) | 2018-06-07 | 2018-06-07 | A kind of plug flow type biomass pool solar energy triplet temperature raising device |
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| Publication Number | Publication Date |
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| CN208485776U true CN208485776U (en) | 2019-02-12 |
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| CN201820883734.2U Expired - Fee Related CN208485776U (en) | 2018-06-07 | 2018-06-07 | A kind of plug flow type biomass pool solar energy triplet temperature raising device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023220228A1 (en) * | 2022-05-11 | 2023-11-16 | Board Of Trustees Of Michigan State University | Oxidation reactor for solid solar thermochemical fuel |
-
2018
- 2018-06-07 CN CN201820883734.2U patent/CN208485776U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023220228A1 (en) * | 2022-05-11 | 2023-11-16 | Board Of Trustees Of Michigan State University | Oxidation reactor for solid solar thermochemical fuel |
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|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190212 Termination date: 20190607 |
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| CF01 | Termination of patent right due to non-payment of annual fee |