CN204737952U - From multizone biogas fermentation system who lives and flow and stir - Google Patents
From multizone biogas fermentation system who lives and flow and stir Download PDFInfo
- Publication number
- CN204737952U CN204737952U CN201520181372.9U CN201520181372U CN204737952U CN 204737952 U CN204737952 U CN 204737952U CN 201520181372 U CN201520181372 U CN 201520181372U CN 204737952 U CN204737952 U CN 204737952U
- Authority
- CN
- China
- Prior art keywords
- fermentation
- district
- water shoot
- gas storage
- water pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- 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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a from multizone biogas fermentation system who lives and flow and stir, it is including the fermentation cell body, between water pressure, the drain pipe, the gas storage board, the last lateral wall of fermentation cell body passes through the drain pipe and is connected within a definite time with water pressure, the gas storage board is fixed in in the fermentation chamber through strutting arrangement, the lateral wall that the gas storage board is close to the feed inlet keeps off the gas board for the feed inlet, the lateral wall that the gas storage board is close to the discharge gate keeps off the gas board for the discharge gate, the feed inlet keeps off and still is provided with a plurality of baffles between gas board and the discharge gate fender gas board, advance / discharge gate keeps off between gas board and the adjacent baffle or forms a fermentation between the adjacent baffle and distinguish, every fermentation district top all is provided with independent air duct, the fermentation system still includes the pull rod, and the pull rod comprises horizontal pole, montant, and the pull rod is placed in fermentation chamber and two montants are arranged in the clearance between gas storage board and the fermentation cell body.
Description
Technical field
The present invention relates to a kind of methane fermentation system.
Background technology
The methane-generating pit latest national standards issued for 2002 comprises 5 kinds of pond types, i.e. hydraulic type cylinder methane-generating pit, separation float cover type biogas generating pit, meandering distribution methane-generating pit, prefabricated section (round shape) methane-generating pit and elliposoidal methane-generating pit; Cylinder methane-generating pit had both been pipeline type methane-generating pit, and fermentation raw material enters fermentation in fermentation pipeline and produces biogas, and in fermentation pipeline inner accumulated, easily caused the obstruction of fermentation pipeline; If obstructive position is comparatively dark, usually adopts all foreign material removed in fermentation pipeline, then stab cylinder by the body of rod.
The methane fermentation system that the present invention adopts, employing be pipeline type fermentation system, it can avoid blocking completely, and mode manually can promote being uniformly distributed of fermentation raw material, and it is convenient to remove natural pond slag.
Summary of the invention
The problems such as technical problem to be solved by this invention is, existing pipeline type methane-generating pit easily blocks, and fermentation raw material, strains'distribution are uneven, natural pond liquid poor fluidity.
The present invention is for solving the problems of the technologies described above, and the technical scheme of employing is.
From the multizone methane fermentation system that flowing of living is stirred, it comprises fermentation vat body, water pressure house, water shoot, gas storage plate, fermentation chamber is provided with in fermentation vat body, two corresponding sidewalls are provided with the opening for feed be connected with the chamber that ferments and discharge port about fermentation vat body, the upper side wall of fermentation vat body is connected with water pressure house by water shoot, the surrounding of gas storage plate and top seal and its lower ending opening, gas storage plate is fixed on fermentation chamber indoor by bracing or strutting arrangement, the top sidewall of the top sidewall of gas storage plate and lower sidewalls and fermentation vat body and lower sidewalls have gap, gas storage plate is opening for feed gas block panel near the sidewall of opening for feed, gas storage plate is discharge port gas block panel near the sidewall of discharge port, multiple baffle plate is also provided with between opening for feed gas block panel and discharge port gas block panel, the region formed between opening for feed gas block panel and adjacent baffle plate is the first fermentation zone, the region formed between adjacent baffle plate is the second fermentation zone, region between discharge port gas block panel and adjacent baffle plate is the 3rd fermentation zone, top, each fermentation zone is provided with independently airway, water shoot comprises first district's water shoot, the 3rd district's water shoot, and first district's water shoot is just to the first fermentation zone, and the 3rd district's water shoot is just to the 3rd fermentation zone, fermentation system also comprises pull bar, and described pull bar is by cross bar, and montant forms, the montant of cross bar at least on one end vertical connecting direction, and it is indoor and in the gap that two montants are between gas storage plate and fermentation vat body that pull bar is positioned over fermentation chamber, first district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, the 3rd district's water shoot is provided with the check valve of the unidirectional inflow water pressure house of natural pond liquid controlling fermentation chamber indoor.
The further improvement of such scheme.
The projecting length of baffle plate in the vertical direction is less than the length of opening for feed gas block panel and the projection of discharge port gas block panel in the vertical direction.
The further improvement of such scheme.
The both end sides of above-mentioned cross bar is connected to vertical montant, and montant top is provided with and is connected with hand-held pole between two montants, leaves gap between hand-held pole.
The further improvement of such scheme.
Cross bar section shape adopt T-type structure.
The further improvement of such scheme.
Water pressure house adopts sealed structure, and water pressure house is connected with vapor pipe.
The further improvement of such scheme.
Above-mentioned bracing or strutting arrangement is be arranged at four back up pads fixing on fermentation chamber four corners.
The further improvement of such scheme.
Above-mentioned bracing or strutting arrangement is the column being arranged at fermentation chamber middle part.
The invention has the advantages that: by the obstructing problem moving back and forth thoroughly solution pipeline type fermentation unit of pull bar, and can promote that fermentation raw material gos deep in fermentation system, promote the mobility of natural pond liquid, drive being uniformly distributed of bacterial classification; Fermentation system fermentation efficiency of the present invention is high, and gas production rate is large, clog-free, is applicable to promoting the use of.
Accompanying drawing explanation
In order to be illustrated more clearly in the embodiment of the present invention, simple introduction is done below by the accompanying drawing used required in embodiment, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is perspective view of the present invention.
Fig. 2 is perspective view of the present invention.
Fig. 3 is the fiting relation figure of fermentation vat body of the present invention and pull bar and water pressure house.
Fig. 4 is cross-sectional view of the present invention.
Fig. 5 is the first embodiment perspective view of pull bar of the present invention.
Fig. 6 is pull bar the second embodiment perspective view of the present invention.
Fig. 7 is the drain structure schematic diagram that fermentation vat body of the present invention is arranged.
Fig. 8 is the cross bar cross-sectional view of pull bar of the present invention.
Be denoted as in figure:
10, fermentation vat body; 12, opening for feed; 14, discharge port; 16, ferment chamber; 18, back up pad.
20, water pressure house; 22, vapor pipe.
30, water shoot; 32, first district's water shoot; 34, second district's water shoot; 36, the 3rd district's water shoot.
40, gas storage plate; 42, airway; 44, opening for feed gas block panel; 45, the first baffle plate; 46, second baffle; 47, discharge port gas block panel.
50, pull bar; 51, cross bar; 52, montant; 53, hand-held pole.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, be clearly and completely described the technical scheme in the embodiment of the present invention, obviously, described embodiment is only the present invention's part embodiment, instead of whole embodiment.Based on the embodiment in the present invention, those of ordinary skill in the art are not making under creative work prerequisite, and the every other embodiment obtained, all belongs to scope.
As Fig. 1, 2, 3, shown in 4, from the multizone methane fermentation system that flowing of living is stirred, primarily of fermentation vat body 10, water pressure house 20, water shoot 30, gas storage plate 40 forms, fermentation vat body 10 and be connected with water shoot 30 between water pressure house 20, gas storage plate 40 is arranged in fermentation vat body 10, fermentation raw material enters fermentation in fermentation vat body 10 and produces biogas, natural pond liquid in extruding fermentation vat body 10 flows in water pressure house 20 by water shoot 30, when using the biogas stored in fermentation vat body 10, the natural pond liquid stored in water pressure house flows in fermentation vat body 10 by water shoot 30 again, complete circulating of natural pond liquid.
Fermentation chamber 16 is provided with in fermentation vat body 10, the corresponding sidewall of fermentation vat body about 10 two is provided with the opening for feed 12 be connected with the chamber 16 that ferments and discharge port 14, four corners of fermentation chamber 16 are fixed with four back up pads 18, the horizontal plane at back up pad 18 lower-most point place, higher than fermentation chamber 16 bottom surface more than 10cm, facilitates fermentation raw material flowing in fermentation chamber 16.
The surrounding of gas storage plate 40 and top seal and its lower ending opening, gas storage plate 40 adapts with fermentation chamber 16 shape of fermentation vat body 10 and is fixed in back up pad 18, gas storage plate 40 is opening for feed gas block panel 44 near the sidewall of opening for feed 12, and gas storage plate 40 is discharge port gas block panel 47 near the sidewall of discharge port 14; Preferably, two baffle plates are also provided with between opening for feed gas block panel 44 and discharge port gas block panel 47, be respectively the first baffle plate 45 and second baffle 46, the width of gas storage plate 40 is less than the width of the fermentation chamber 16 of fermentation vat body 10, and namely the top sidewall of gas storage plate 40 and the top sidewall of lower sidewalls and fermentation vat body 10 and lower sidewalls have interval.
The region formed between opening for feed gas block panel 44 and the first baffle plate 45 is the first fermentation zone, the region formed between first baffle plate 45 and second baffle 46 is the second fermentation zone, region between second baffle 46 and discharge port gas block panel 47 is the 3rd fermentation zone, for making full use of the space in gas storage plate 40, the projecting length of the first baffle plate 45, second baffle 46 in the vertical direction is less than the length of opening for feed gas block panel 44 and the projection of discharge port gas block panel 47 in the vertical direction.
First fermentation zone, the second fermentation zone and the 3rd top, fermentation zone are provided with separate airway 42, are exported the biogas stored in the first fermentation zone, the second fermentation zone and the 3rd fermentation zone by airway 42 respectively.
Water shoot 30 is connected with between sidewall and water pressure house 20 above fermentation vat body 10, water shoot 30 comprises first district's water shoot 32, second district's water shoot 34, the 3rd district's water shoot 36, first district's water shoot 32 is just to the first fermentation zone, second district's water shoot 34 is just to the second fermentation zone, and the 3rd district's water shoot 36 is just to the 3rd fermentation zone; For ensureing the obstruction of water shoot and ensureing that natural pond liquid flowing is smooth and easy, first district's water shoot, second district's water shoot and the 3rd district's water shoot are set to two respectively.
Water pressure house 20 top seal and water pressure house 20 top is connected with the vapor pipe be communicated with air.
Fermentation raw material enters in fermentation chamber 16 also to ferment by opening for feed 12 and produces biogas, the biogas produced is gathered in the first fermentation zone, the second fermentation zone and the 3rd fermentation zone respectively, the biogas assembled in gas storage plate 40 occupies the space of natural pond liquid in gas storage plate, and extruding natural pond liquid convection current also makes the natural pond liquid liquid level fermented in chamber 16 rise, due to bacterial classification, fermentation raw material equal distribution is uneven, cause the difference of fermentation efficiency in each fermentation zone and gas production rate, suppose that the gas producing efficiency of the second fermentation zone is high and gas production rate is large, first full biogas is collected in second fermentation zone, the biogas continuing fermentation generation in second fermentation zone flows to the first fermentation zone and the second fermentation zone respectively, until the first fermentation zone, second fermentation zone and the 3rd fermentation zone are mutually all collected full biogas and are interconnected, until collect full biogas in gas storage plate, the biogas continuing fermentation generation again will by flowing into fermentation system outside bottom opening for feed gas block panel and discharge port gas block panel, collect in process of methane in gas storage plate 40, natural pond liquid liquid level constantly rises, and the horizontal plane that natural pond liquid liquid level reaches water shoot 30 lower-most point place is, the natural pond liquid stored in fermentation chamber 16 is flowed in water pressure house by water shoot.
The airway 42 separate by the first fermentation zone, the second fermentation zone, the 3rd top, fermentation zone externally exports biogas, biogas air pressure in gas storage plate 40 declines, the natural pond liquid stored in water pressure house is back in fermentation chamber 16 by water shoot 30, supplements the biogas volume lacked.
Fermentation raw material enters in fermentation chamber 16, there is the possibility of blocking, can be solved easily if blocked in opening for feed and discharge port by rod, but if blocked in the first baffle plate or second baffle position, will be difficult to cleaning.
For thoroughly solving above-mentioned obstructing problem, this fermentation system also comprises pull bar 50, described pull bar 50 is by cross bar 51, montant 52 forms, the both end sides of cross bar 51 is connected to vertical montant 52, montant 52 top is provided with and is connected with hand-held pole 53 between two montant 52, preferably, leaves gap between hand-held pole 53.
Pull bar 50 is positioned in fermentation chamber 16 and two montants 52 lay respectively in the gap between gas storage plate 40 and fermentation vat body 10, pull bar 50 is driven to move by pulling hand-held pole 53, effectively can solve the obstructing problem in fermentation chamber 16, and fermentation raw material can be promoted in pull bar 50 moving process to go deep in fermentation system and be uniformly distributed, the flowing of natural pond liquid can also be promoted, thus promote being uniformly distributed of bacterial classification.
As shown in Figure 6, the another kind of embodiment of pull bar 50, the end side of cross bar 51 connects vertical montant 52, the hand-held pole 53 of montant 52 top level connection joint one and cross bar 51 same side, and this embodiment, can conveniently take out pull bar 50; Pull bar 50 is put into along the gap between fermentation vat body 10 and gas storage plate 40 chamber 16 that ferments, by pulling hand-held pole 53, solving and block or drive being uniformly distributed of fermentation raw material, promote natural pond liquid flowing, drive bacterial classification to be uniformly distributed.
As shown in Figure 8, for increasing the contact area of cross bar 51, the section shape of cross bar 51 adopts T-type structure.
The present invention can adopt other bracing or strutting arrangements, and such as adopt column to be arranged at fermentation chamber middle part, above-mentioned pull bar 50 preferably adopts the second embodiment, and cross bar 51 length of pull bar 50 should be less than the distance of column and the indoor sidewall of fermentation chamber.
Existing hydraulic methane fermentation system natural pond liquid self-circulation ability, bacterial classification is uniformly distributed can not effectively to utilize the flowing of natural pond liquid to promote, thus cause the fermentation efficiency of fermentation system low, gas production rate is low, for promoting the natural pond of the present invention liquid recycle stream property moved and promoting being uniformly distributed of bacterial classification, the present invention adopts multiple technologies scheme.
The first scheme.
The horizontal plane in the 3rd water shoot lower-most point place, district is lower than the horizontal plane at the second water shoot lower-most point place, district, and the horizontal plane at the second water shoot lower-most point place, district is lower than the horizontal plane at the first water shoot lower-most point place, district.
Fermentation raw material enters the indoor fermentation of fermentation chamber and produces biogas, and accumulate in gas storage plate, occupy the space in gas storage plate, and the natural pond liquid extruded below gas storage plate first flows in water pressure house by the 3rd district's water shoot, because the 3rd district's water shoot is near discharge port, the natural pond liquid in the 3rd fermentation zone is rich in bacterial classification; Along with the methane quantity of the indoor generation of fermentation chamber is larger, the natural pond liquid flowed in water pressure house in fermentation chamber is more, when the natural pond liquid liquid level stored in water pressure house reaches the horizontal plane at the second water shoot lower-most point place, district, the natural pond liquid of fermentation chamber indoor flows in water pressure house by second district's water shoot again; Similarly, when the natural pond liquid liquid level stored in water pressure house reaches the horizontal plane at the first water shoot lower-most point place, district, the natural pond liquid of fermentation chamber indoor is flowed in water pressure house by first district's water shoot again.
Because the first fermentation zone is near opening for feed, the foreign material contained in first fermentation zone are more, first by the 3rd district's water shoot, the natural pond liquid being rich in bacterial classification in the 3rd fermentation zone is flowed in water pressure house, again in natural pond liquid reflux course, can effectively promote that bacterial classification is uniformly distributed, and not easily cause water shoot to block.
First scheme.
First district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, 3rd district's water shoot is provided with the check valve of the unidirectional inflow water pressure house of natural pond liquid controlling fermentation chamber indoor, first district's water shoot lower-most point and the 3rd district's water shoot lower-most point are positioned on same horizontal plane, and the horizontal plane at the second water shoot lower-most point place, district is higher than the horizontal plane at the first water shoot lower-most point place, district.
Fermentation raw material enters the indoor fermentation of fermentation chamber and produces biogas, and accumulate in gas storage plate, occupy the space in gas storage plate, and the natural pond liquid extruded below gas storage plate is first by the unidirectional inflow water pressure house of the 3rd district's water shoot, because the 3rd district's water shoot is near discharge port, the natural pond liquid in the 3rd fermentation zone is rich in bacterial classification to be brought in water pressure house; Along with the methane quantity of gas storage plate inner accumulated is larger, it is more that natural pond liquid below gas storage plate flows into water pressure house, when the natural pond liquid liquid level stored in water pressure house reaches the horizontal plane at the second water shoot lower-most point place, district, fermentation chamber indoor natural pond liquid can be flowed in water pressure house by second district's water shoot.
When externally exporting biogas by airway, the biogas volume of gas storage board memory storage declines, and the natural pond liquid stored in water pressure house is first back to fermentation chamber indoor by unidirectional being back in fermentation chamber and by second district's water shoot of first district's water shoot; When the horizontal plane of the natural pond liquid liquid level stored in water pressure house lower than the second water shoot lower-most point place, district, the natural pond liquid in water pressure house can only be back in fermentation chamber by first district's water shoot is unidirectional, thus completes circulating of natural pond liquid.
Its advantage is: in the first fermentation zone, foreign material are more, by the control of check valve, foreign material can be avoided to enter in water pressure house, and the natural pond liquid in the 3rd fermentation zone is rich in bacterial classification, when natural pond liquid in water pressure house refluxes, can the bacterial classification be rich in be brought in the first fermentation zone, promote being uniformly distributed of bacterial classification, improve the fermentation efficiency in fermentation system.
The third scheme.
First district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, second district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, the 3rd district's water shoot is provided with the check valve of the unidirectional inflow water pressure house of natural pond liquid controlling fermentation chamber indoor.
Fermentation raw material enters the indoor fermentation of fermentation chamber and produces biogas, and accumulate in gas storage plate, occupy the space in gas storage plate, and the natural pond liquid extruded below gas storage plate is by the unidirectional inflow water pressure house of the 3rd district's water shoot, because the 3rd district's water shoot is near discharge port, the natural pond liquid in the 3rd fermentation zone is rich in bacterial classification to be brought in water pressure house; When the biogas that gas storage board memory stores up externally being exported by airway, in gas storage plate, biogas air pressure declines, the natural pond liquid stored in water pressure house ferments in chamber by first district's water shoot and unidirectional being back to of second district's water shoot, and the natural pond liquid being rich in bacterial classification is brought in the first fermentation zone and the second fermentation zone, promote being uniformly distributed of bacterial classification.
4th kind of scheme.
First district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, second district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, the horizontal plane at the 3rd minimum place of district's water shoot is higher than the horizontal plane at first district's water shoot and the second water shoot lower-most point place, district.
Fermentation raw material enters the indoor fermentation of fermentation chamber and produces biogas, and accumulate in gas storage plate, occupy the space in gas storage plate, and the natural pond liquid extruded below gas storage plate flows in water pressure house by the 3rd district's water shoot, because the 3rd district's water shoot is near discharge port, the natural pond liquid in the 3rd fermentation zone is rich in bacterial classification to be brought in water pressure house; When the biogas that gas storage board memory stores up externally being exported by airway, in gas storage plate, biogas air pressure declines, the natural pond liquid stored in water pressure house ferments in chamber by first district's water shoot and unidirectional being back to of second district's water shoot, and the natural pond liquid being rich in bacterial classification is brought in the first fermentation zone and the second fermentation zone, promote being uniformly distributed of bacterial classification.
Its advantage is: the 3rd district's water shoot is not provided with check valve, utilizes the lowest point of the 3rd district's water shoot higher than first district's water shoot and second district's water shoot lower-most point, can bring in the first fermentation zone and the second fermentation zone by the natural pond liquid being rich in bacterial classification; If when the lower-most point of first district's water shoot is lower than second district's water shoot lower-most point, the more natural pond liquid being rich in bacterial classification, by inflow first fermentation zone, improves the fermentation efficiency of the first fermentation zone; Similarly, when the horizontal plane at the lower-most point place of first district's water shoot is higher than second district's water shoot lower-most point, the natural pond liquid being rich in bacterial classification more in water pressure house, by inflow second fermentation zone, improves the fermentation efficiency of the second fermentation zone.
5th kind of scheme.
Omit second district's water shoot, first district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, the 3rd district's water shoot is provided with the check valve of the unidirectional inflow water pressure house of natural pond liquid controlling fermentation chamber indoor.
Fermentation raw material enters the indoor fermentation of fermentation chamber and produces biogas, and accumulate in gas storage plate, occupy the space in gas storage plate, and the natural pond liquid extruded below gas storage plate is by the unidirectional inflow water pressure house of the 3rd district's water shoot, because the 3rd district's water shoot is near discharge port, the natural pond liquid in the 3rd fermentation zone is rich in bacterial classification to be brought in water pressure house; When the biogas that gas storage board memory stores up externally being exported by airway, in gas storage plate, biogas air pressure declines, the natural pond liquid stored in water pressure house is by first district's water shoot unidirectional inflow first fermentation zone, and a large amount of bacterial classifications is brought in the first fermentation zone, promote being uniformly distributed of bacterial classification, and the circulating of natural pond liquid.
To the above-mentioned explanation of the disclosed embodiments, professional and technical personnel in the field are realized or uses the present invention.To be apparent for those skilled in the art to the multiple amendment of these embodiments, the General Principle defined in the present invention when not departing from spirit of the present invention or scope, can realize in other embodiments.Therefore, the present invention can not be defined to these embodiments shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.
Claims (4)
1. from the multizone methane fermentation system that flowing of living is stirred, it is characterized in that, it comprises fermentation vat body, water pressure house, water shoot, gas storage plate, fermentation chamber is provided with in fermentation vat body, two corresponding sidewalls are provided with the opening for feed be connected with the chamber that ferments and discharge port about fermentation vat body, the upper side wall of fermentation vat body is connected with water pressure house by water shoot, the surrounding of gas storage plate and top seal and its lower ending opening, gas storage plate is fixed on fermentation chamber indoor by bracing or strutting arrangement, the top sidewall of the top sidewall of gas storage plate and lower sidewalls and fermentation vat body and lower sidewalls have gap, gas storage plate is opening for feed gas block panel near the sidewall of opening for feed, gas storage plate is discharge port gas block panel near the sidewall of discharge port, multiple baffle plate is also provided with between opening for feed gas block panel and discharge port gas block panel, the region formed between opening for feed gas block panel and adjacent baffle plate is the first fermentation zone, the region formed between adjacent baffle plate is the second fermentation zone, region between discharge port gas block panel and adjacent baffle plate is the 3rd fermentation zone, top, each fermentation zone is provided with independently airway, water shoot comprises first district's water shoot, the 3rd district's water shoot, and first district's water shoot is just to the first fermentation zone, and the 3rd district's water shoot is just to the 3rd fermentation zone, fermentation system also comprises pull bar, and described pull bar is by cross bar, and montant forms, the montant of cross bar at least on one end vertical connecting direction, and it is indoor and in the gap that two montants are between gas storage plate and fermentation vat body that pull bar is positioned over fermentation chamber, first district's water shoot is provided with the check valve of the natural pond liquid unidirectional inflow fermentation chamber room controlled in water pressure house, the 3rd district's water shoot is provided with the check valve of the unidirectional inflow water pressure house of natural pond liquid controlling fermentation chamber indoor, the projecting length of baffle plate in the vertical direction is less than the length of opening for feed gas block panel and the projection of discharge port gas block panel in the vertical direction, above-mentioned bracing or strutting arrangement is the column being arranged at fermentation chamber middle part.
2. the multizone methane fermentation system stirred from flowing of living according to claim 1, it is characterized in that, the end side of above-mentioned cross bar is connected with vertical montant, and montant top is provided with montant.
3. according to claim 2 from live flowing stir multizone methane fermentation system, it is characterized in that, cross bar section shape adopt T-type structure.
4. the multizone methane fermentation system stirred from flowing of living according to claim 3, it is characterized in that, water pressure house adopts sealed structure, and water pressure house is connected with vapor pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520181372.9U CN204737952U (en) | 2015-03-30 | 2015-03-30 | From multizone biogas fermentation system who lives and flow and stir |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520181372.9U CN204737952U (en) | 2015-03-30 | 2015-03-30 | From multizone biogas fermentation system who lives and flow and stir |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204737952U true CN204737952U (en) | 2015-11-04 |
Family
ID=54419697
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520181372.9U Expired - Fee Related CN204737952U (en) | 2015-03-30 | 2015-03-30 | From multizone biogas fermentation system who lives and flow and stir |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204737952U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104818204A (en) * | 2015-03-30 | 2015-08-05 | 陆永成 | Self-activation flow stirring multi-zone biogas fermentation system |
-
2015
- 2015-03-30 CN CN201520181372.9U patent/CN204737952U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104818204A (en) * | 2015-03-30 | 2015-08-05 | 陆永成 | Self-activation flow stirring multi-zone biogas fermentation system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN204737952U (en) | From multizone biogas fermentation system who lives and flow and stir | |
CN204737954U (en) | Clog -free biogas fermentation system of pull stirring type | |
CN204714794U (en) | From flowing anti-blocking methane fermentation system of living | |
CN204702748U (en) | Promote the efficient methane fermentation system of natural pond liquid turbulent flow | |
CN204752702U (en) | Water pressure formula biogas fermentation system of barometric disturbance stirring | |
CN204737953U (en) | High -efficient biogas fermentation system based on natural pond liquid self -loopa technique | |
CN104726324A (en) | Self-activating flowing blockage-preventing biogas fermenting system | |
CN204752703U (en) | Clog -free water pressure formula of linear type fermentation system that flows from living and stir | |
CN204714792U (en) | The clog-free methane fermentation system of ultra-high efficiency hydraulic pipeline type | |
CN104789458B (en) | Promote strain equally distributed from flowing agitating type marsh gas fermenting system of living | |
CN104726323A (en) | Efficient biogas fermentation system based on biogas slurry self-circulation technology | |
CN204714793U (en) | Promote that bacterial classification is equally distributed from flowing stirring-type methane fermentation system of living | |
CN104818205A (en) | High efficiency biogas fermentation system for promoting turbulent flow of biogas slurry | |
CN104818204A (en) | Self-activation flow stirring multi-zone biogas fermentation system | |
CN104818203A (en) | Pull stirring type non-blocking biogas fermentation system | |
CN104818206A (en) | Barometric disturbance stirring hydraulic biogas fermentation system | |
CN204702747U (en) | Ultra-high efficiency hydraulic methane fermentation system | |
CN204509283U (en) | Shape of a hoof ultra-high efficiency anaerobic ferment devices | |
CN204918576U (en) | Fermentation system is imitated to shape of a hoof natural pond liquid circulatory flow dynamic formula superelevation | |
CN104789457A (en) | Self-activated flow-stirred linear non-blocking hydraulic fermentation system | |
CN204509296U (en) | Assembly type shape of a hoof natural pond liquid sinuous flow drives the ultra-high efficiency biogas generation systems of cloth bacterium | |
CN204509282U (en) | The some subregions of the shape of a hoof promote the ultra-high efficiency biogas generation systems of natural pond liquid sinuous flow | |
CN204509286U (en) | Air pressure promotes the ultra-high efficiency anaerobic fermentation system of natural pond liquid sinuous flow | |
CN204509284U (en) | Some subregions promote the equally distributed anaerobic fermentation system of bacterial classification to flow disturbance | |
CN204509289U (en) | The unidirectional convection agitation of the shape of a hoof promotes the anaerobic fermentation system of feedstock |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151104 Termination date: 20170330 |