CN104611198A - Biogas generation method for assembly-type U-shaped biogas-slurry-turbulence biogas generation system - Google Patents

Biogas generation method for assembly-type U-shaped biogas-slurry-turbulence biogas generation system Download PDF

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CN104611198A
CN104611198A CN201510030303.2A CN201510030303A CN104611198A CN 104611198 A CN104611198 A CN 104611198A CN 201510030303 A CN201510030303 A CN 201510030303A CN 104611198 A CN104611198 A CN 104611198A
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李俊
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    • C12M21/00—Bioreactors or fermenters specially adapted for specific uses
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    • C12M23/00—Constructional details, e.g. recesses, hinges
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    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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    • C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/14—Pressurized fluid
    • 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

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Abstract

The invention discloses a biogas generation method for an assembly-type U-shaped biogas-slurry-turbulence biogas generation system. The method comprises steps as follows: a fermentation raw material is poured into a U-shaped fermentation pipeline through a feeding pipe and is fermented in the U-shaped fermentation pipeline to produce biogas, the biogas is accumulated in a space between the side wall of the feeding pipe and the side wall of the discharging pipe, and the biogas occupies the space in the fermentation pipeline and squeezes biogas slurry in the fermentation pipeline to flow to the feeding pipe and the discharging pipe and then flow into a hydraulic pressure chamber through a discharging pipe water-discharging pipe in one direction. The biogas stored in the fermentation pipeline is used, and the pressure of the biogas in the fermentation pipeline is reduced, so that the biogas stored in the hydraulic pressure chamber flows back to the fermentation pipeline through a feeding pipe water-discharging pipe in one direction, and circulatory flowing of the biogas slurry is completed; biogas is constantly produced and used with methods A and B, and the circulatory flowing of the biogas slurry is promoted.

Description

The biogas generation systems of assembly type shape of a hoof natural pond liquid sinuous flow produces the method for biogas
Technical field
The present invention relates to a kind of anaerobic ferment devices, particularly a kind of methane fermentation system.
Background technology
The principle of work of traditional methane tank, when producing biogas in pond, the biogas in gas storage is on the increase, and pressure constantly increases, and forces liquid level in main pond to decline, squeezes out a part of feed liquid in water pressure house.When people open cooking stove, the pressure in methane-generating pit declines gradually, and water pressure house feed liquid continues to flow and is back to main pond, and like this, constantly aerogenesis and with gas, makes sweathouse and discharge room maintain pressure equilibrium ground state all the time.
Traditional methane tank fermentative routes is short, natural pond liquid poor fluidity, and strains'distribution is uneven, causes the factor of created gase of whole fermentation system to decline.
Summary of the invention
For solving the deficiencies in the prior art, technical problem to be solved by this invention is that the fermentation efficiency route of traditional methane tank is short, and fermentation efficiency is low, and natural pond liquid convection effects difference causes strains'distribution uneven.
For solving the problems of the technologies described above, the technical solution used in the present invention is.
Assembly type shape of a hoof natural pond liquid sinuous flow drives the ultra-high efficiency biogas generation systems of cloth bacterium, be made up of feed-pipe, discharge nozzle, U-shaped fermentation pipeline, water pressure house, feed-pipe and the dismountable insertion of discharge nozzle U-shaped fermentation pipeline both end sides and feed-pipe sidewall and discharge nozzle sidewall go deep in U-shaped fermentation pipeline, water pressure house is positioned over U-shaped fermentation pipeline top, the feed-pipe water shoot of horizontal positioned is connected with between water pressure house and feed-pipe, be connected with the discharge nozzle water shoot of horizontal positioned between water pressure house and discharge nozzle, U-shaped fermentation pipeline is provided with airway; Feed-pipe water shoot is provided with the check valve controlling liquid unidirectional inflow feed-pipe in natural pond in water pressure house, discharge nozzle water shoot is provided with the check valve controlling liquid unidirectional inflow water pressure house in natural pond in discharge nozzle.
The further improvement of technique scheme.
The projecting length of the sidewall in the vertical direction that feed-pipe and discharge nozzle go deep in U-shaped fermentation pipeline is less than 2/3rds of U-shaped fermentation pipeline vertical direction height.
The further improvement of technique scheme.
Water pressure house top adopts sealed structure and water pressure house top is also communicated with the vapor pipe be communicated with air.
The further improvement of technique scheme.
Described airway has multiple, and is interconnected; When preventing one of them airway from blocking occurring, other airways can also normally use.
The biogas generation systems of assembly type shape of a hoof natural pond liquid sinuous flow produces the method for biogas, and its step comprises:
A, fermentation raw material to be poured in U-shaped fermentation pipeline by feed-pipe and fermentation produces biogas in U-shaped fermentation pipeline, in the space of methane accumulation between feed-pipe sidewall and discharge nozzle sidewall, biogas occupies space in fermentation pipeline and the natural pond liquid that extruding is fermented in pipeline flows in feed-pipe and discharge nozzle, by the unidirectional inflow water pressure house of discharge nozzle water shoot;
B, the biogas using fermentation pipeline internal memory to store up, the biogas air pressure in fermentation pipeline declines, and the natural pond liquid stored is fermented in pipeline by unidirectional being back to of feed-pipe water shoot, complete circulating of natural pond liquid in water pressure house;
C, constantly to produce biogas according to the method for above-mentioned A, B and use biogas, promoting circulating of natural pond liquid.
Above-mentioned fermentation raw material can be animal excrement, stalk, sewage etc.
The present invention is relative to the advantage of prior art: utilize U-shaped fermentation pipeline to increase fermentation path, extrude circulating of natural pond liquid, do not need manual intervention, reduce the operation easier of fermentation equipment in marsh gas fermentation processes; The insert mode of connection of feed-pipe and discharge nozzle and U-shaped fermentation pipeline, replaces traditional feed-pipe gas block panel and discharge nozzle gas block panel, convenient charging and discharging, and the difficulty reducing production, and the cleaning etc. of pond body.
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 vertical view of the present invention.
Fig. 2 is A-A diagrammatic cross-section of the present invention.
Fig. 3 is B-B diagrammatic cross-section of the present invention.
Fig. 4 is C-C diagrammatic cross-section of the present invention.
Be denoted as in figure:
10, feed-pipe; 12 feed-pipe water shoots.
20, discharge nozzle; 22 discharge nozzle water shoots.
30, ferment pipeline; 32, airway; 34, gas block panel.
40, water pressure house; 42, vapor pipe.
50, cloth bacterium device; 51, water shoot; 52, cloth tube road.
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 shown in Figure 1, assembly type shape of a hoof natural pond liquid sinuous flow drives the ultra-high efficiency biogas generation systems of cloth bacterium, it is primarily of feed-pipe 10, discharge nozzle 20, fermentation pipeline 30, water pressure house 40 is formed, fermentation pipeline 30 is U-shaped fermentation pipeline, the section shape of U-shaped fermentation pipeline can be original shape, rectangle, the geometrical shapies such as ellipse, and U ferments, pipeline 30 end positions is provided with the socket matched with feed-pipe 10 and discharge nozzle 20 to U-shaped fermentation pipeline 30 horizontal positioned, the two ends of feed-pipe 10 and the dismountable insertion of discharge nozzle 20 U-shaped fermentation the pipeline 30 and sidewall of feed-pipe 10 and discharge nozzle 20 gos deep into the natural pond liquid liquid level of U-shaped fermentation pipeline 30 with upper/lower positions, replace traditional feed-pipe gas block panel and discharge nozzle gas block panel, in U-shaped fermentation pipeline 30, fermentation generation biogas is collected between feed-pipe sidewall and discharge nozzle sidewall, when the biogas amount of gathering is greater than the saturation of feed-pipe sidewall and discharge nozzle sidewall, unnecessary biogas will overflow from feed-pipe sidewall and discharge nozzle sidewall bottom, water pressure house 40 is positioned over U-shaped fermentation pipeline 30 top, is connected with the feed-pipe water shoot 12 of horizontal positioned between water pressure house 40 and feed-pipe 10, is connected with the discharge nozzle water shoot 22 of horizontal positioned between water pressure house 40 and discharge nozzle 20, in U-shaped fermentation pipeline 30, fermentation produces biogas, and biogas occupies the space in U-shaped fermentation pipeline 30, and the natural pond liquid extruded in U-shaped fermentation pipeline flows in water pressure house 40 by feed-pipe water shoot 12 and discharge nozzle water shoot, when using the biogas of fermentation pipeline internal memory storage, the biogas air pressure in U-shaped fermentation pipeline declines, and the natural pond liquid stored in water pressure house 40 is back in fermentation pipeline by feed-pipe water shoot 12 and discharge nozzle water shoot 22, completes circulating of natural pond liquid.
Water pressure house 40 top adopts sealed structure, prevent foreign material from falling in water pressure house and cause obstruction, and water pressure house 40 top is provided with a vapor pipe be communicated with air, ensures that water pressure house 40 internal gas pressure is consistent with external pressure.
Feed-pipe 10, discharge nozzle 20, U-shaped fermentation pipeline 30 and water pressure house 40 all can adopt concrete placement or adopt PVC pipeline to connect makes or adopts glass-reinforced plastic material to make.
Feed-pipe 10 and discharge nozzle 20 removably connect with U-shaped fermentation pipeline 30, not only convenient transport, ease of assembly, and reduce manufacture difficulty and cost, when feed-pipe tilts to insert U-shaped fermentation pipeline, convenient charging, the flowing of natural pond liquid is utilized to be more prone to promote charging, when discharge nozzle tilts to insert U-shaped fermentation pipeline, convenient discharging, more easily draws slag.
The natural pond liquid poor mobile performance of traditional hydraulic type biomass pool, fermentation raw material not easily gos deep into fermentation system inside, strains'distribution is uneven, reduce the fermentation efficiency of whole fermentation system, and existing U-shaped fermentation system or S type fermentation system, although the short problem of the fermentative routes solving traditional methane fermentation system, the flowing of natural pond liquid is stirred and is still needed manual intervention, makes peasant household use biogas inconvenient.
The present invention devises the scheme of multiple promotion natural pond liquid flowing, drives being uniformly distributed of bacterial classification, and promote charging by the flowing of natural pond liquid, the fermentation efficiency of whole fermentation system is improved, in the flow process of natural pond liquid, does not need artificial intervention, use biogas is convenient, and concrete scheme is as follows.
The first promotes the scheme (hereinafter referred to as the first scheme) that natural pond liquid flowing is stirred.
Feed-pipe water shoot is provided with the check valve controlling liquid unidirectional inflow feed-pipe in natural pond in water pressure house, discharge nozzle water shoot is provided with the check valve controlling liquid unidirectional inflow water pressure house in natural pond in discharge nozzle.
Fermentation raw material to be entered in fermentation system by feed-pipe and fermentation produces biogas in U-shaped fermentation pipeline, biogas is collected in U-shaped fermentation pipeline, occupy the space in U-shaped fermentation pipeline, extruding the natural pond liquid in U-shaped fermentation pipeline flows in feed-pipe and discharge nozzle by the bottom of feed-pipe sidewall and the bottom of discharge nozzle sidewall, along with the increase of biogas air pressure, the natural pond liquid liquid level in feed-pipe and discharge nozzle constantly rises; Under the control of check valve, the natural pond liquid being rich in bacterial classification near discharge nozzle by the unidirectional inflow water pressure house of discharge nozzle water shoot, and is brought in water pressure house by the natural pond liquid in U-shaped fermentation pipeline; During the biogas using U-shaped fermentation pipeline internal memory to store up, biogas air pressure in U-shaped fermentation pipeline declines, the natural pond liquid stored in water pressure house is back in U-shaped fermentation pipeline by discharge nozzle water shoot is unidirectional, in natural pond liquid reflux course in water pressure house, the natural pond liquid being rich in bacterial classification is brought in feed-pipe, and drives fermentation raw material to go deep into fermentation system inside by the natural pond liquid of flowing; What utilize natural pond liquid circulates stirring, promotes the fermentation efficiency of whole fermentation system.
The second promotes the scheme (hereinafter referred to as first scheme) that natural pond liquid flowing is stirred.
Feed-pipe water shoot is provided with the check valve controlled in water pressure house in the unidirectional inflow feed-pipe of natural pond liquid, the horizontal plane at the extreme lower position place of discharge nozzle water shoot is higher than the horizontal plane at feed-pipe water shoot lower-most point place.
Fermentation raw material to be entered in fermentation system by feed-pipe and fermentation produces biogas in U-shaped fermentation pipeline, biogas is collected in U-shaped fermentation pipeline, occupy the space in U-shaped fermentation pipeline, extruding the natural pond liquid in U-shaped fermentation pipeline flows in feed-pipe and discharge nozzle by the bottom of feed-pipe sidewall and the bottom of discharge nozzle sidewall, along with the increase of biogas air pressure, the natural pond liquid liquid level in feed-pipe and discharge nozzle constantly rises, under the control of feed-pipe water shoot check valve, the natural pond liquid in U-shaped fermentation pipeline flows in water pressure house by discharge nozzle water shoot, and along with the increase of biogas store content in U-shaped fermentation pipeline, in U-shaped fermentation pipeline, the amount of natural pond liquid inflow water pressure house is larger, use the biogas that U-shaped fermentation pipeline internal memory stores up, in U-shaped fermentation pipeline, biogas air pressure declines, the natural pond liquid stored in water pressure house is back in feed-pipe by feed-pipe water shoot is unidirectional, and the natural pond liquid stored in water pressure house can also be back in discharge nozzle by discharge nozzle water shoot, due to the high and low position relation of feed-pipe water shoot and discharge nozzle water shoot, natural pond liquid more in water pressure house is made to be back in feed-pipe by feed-pipe water shoot is unidirectional, and the natural pond liquid that bacteria containing amount is abundant is brought in feed-pipe, the flowing of natural pond liquid is utilized to promote that fermentation raw material flows in fermentation system.
The third promotes the scheme (hereinafter referred to as the third scheme) that natural pond liquid flowing is stirred.
The gas block panel between feed-pipe sidewall and discharge nozzle sidewall is also provided with in fermentation pipeline, gas block panel has one at least, preferably, gas block panel is two, a fermentation zone is formed between entry/exit material pipe sidewall and adjacent gas block panel or between adjacent gas block panel, the projecting length of gas block panel in the vertical direction is less than the length of deeply fermenting in pipeline into/material pipe sidewall, each top, fermentation zone is connected with independently airway 32, mutually be not communicated with between each airway 32, ensure the separate of each fermentation zone, and airway 32 is provided with the valve body controlling airway and open and close.
Entry/exit material pipe sidewall gos deep into the natural pond following length of liquid liquid level in U-shaped fermentation pipeline and is less than 2/3rds of the length on U-shaped fermentation pipeline vertical direction.
Fermentation raw material to be entered in fermentation system by feed-pipe and fermentation produces biogas in U-shaped fermentation pipeline, biogas is collected in each fermentation zone in fermentation pipeline, the biogas gathered in fermentation zone occupies the space in fermentation zone, and the natural pond liquid extruded in fermentation zone flows to adjacent fermentation zone, promote the convection agitation of natural pond liquid, promote bacterial classification to be uniformly distributed in the convection agitation process of natural pond liquid and promote that fermentation raw material flows in fermentation system; Because fermentation raw material, bacterial classification equal distribution are uneven, make the fermentation efficiency of each fermentation zone different, the biogas that the fermentation zone of first collecting full biogas continues to produce is by flowing in adjacent fermentation zone bottom gas block panel, until each fermentation zone in fermentation pipeline is communicated with, and the biogas in common extruding fermentation pipeline flows into feed-pipe and discharge nozzle; Utilize the gas pressure of biogas, promote the convection agitation of natural pond liquid efficiently.
When using the biogas collected in any one fermentation zone, biogas air pressure in this fermentation zone declines, the natural pond liquid of adjacent fermentation zone flows to the fermentation zone of this use biogas, biogas space in U-shaped fermentation pipeline reduces, the natural pond liquid stored in water pressure house is back in fermentation pipeline by feed-pipe water shoot and discharge nozzle water shoot, supplements the biogas space of reducing.
4th kind promotes the scheme (hereinafter referred to as the 4th kind of scheme) that natural pond liquid flowing is stirred.
The basis of the third scheme is improved, the present invention also comprises cloth bacterium device, cloth bacterium device is made up of water shoot, cloth tube road and cloth bacterium hole, water shoot end side connects water pressure house, another side connects cloth tube road, cloth tube road is U-shaped and is fixed in U-shaped fermentation pipeline, cloth tube road extends and extends in each fermentation zone in U-shaped fermentation pipeline, cloth tube road is provided with the cloth bacterium hole that multiple vertical direction runs through, preferably, water shoot is multiple and is distributed in each fermentation zone.
Fermentation raw material enters fermentation in fermentation pipeline and produces biogas in each fermentation zone inner accumulated, biogas occupies the space in fermentation zone, extruding natural pond liquid convection current, and finally flow in feed-pipe, discharge nozzle and cloth bacterium device, along with the increase of biogas air pressure, natural pond liquid in fermentation pipeline is flowed in water pressure house by the water shoot of feed-pipe water shoot, discharge nozzle water shoot and cloth bacterium device, and the natural pond liquid flowing mixing effect in whole fermentation system is enhanced; When using the biogas stored in any one fermentation zone, biogas air pressure in U-shaped fermentation pipeline declines, the natural pond liquid stored in water pressure house is made to be back in fermentation pipeline by the water shoot of feed-pipe water shoot, discharge nozzle water shoot and cloth bacterium device, thus complete circulating of natural pond liquid, drive being uniformly distributed of bacterial classification in the flow process of natural pond liquid, and promote charging.
5th kind promotes the scheme (hereinafter referred to as the 5th kind of scheme) that natural pond liquid flowing is stirred.
The basis of the 4th kind of scheme is improved, feed-pipe water shoot is provided with the check valve controlling liquid unidirectional inflow feed-pipe in natural pond in water pressure house, discharge nozzle water shoot is provided with the check valve controlling liquid unidirectional inflow water pressure house in natural pond in discharge nozzle, the horizontal plane at the water shoot of cloth bacterium device and the lower-most point place of water pressure house link position is higher than the horizontal plane at discharge nozzle water shoot lower-most point place.
In fermentation pipeline, fermentation produces biogas and biogas in each fermentation zone inner accumulated, biogas occupies the space in each fermentation zone, extrude the natural pond liquid convection current bottom each fermentation zone, and first by the unidirectional inflow water pressure house of discharge nozzle water shoot, when the natural pond liquid liquid level stored in water pressure house reaches the lower-most point of the water shoot of cloth bacterium device and water pressure house link position, natural pond liquid in fermentation pipeline can also be flowed in water pressure house by the water shoot of cloth bacterium device, and the natural pond liquid whipping performance in whole fermentation pipeline is enhanced; When using the biogas stored in any one fermentation zone, the biogas air pressure of fermentation pipeline internal memory storage declines, the natural pond liquid stored in water pressure house is made to be back in feed-pipe by feed-pipe water shoot is unidirectional and is back in fermentation pipeline by the water shoot of cloth bacterium device, when the lower-most point of the natural pond liquid liquid level stored in water pressure house lower than the water shoot of cloth bacterium device and water pressure house link position, the natural pond liquid stored in water pressure house is by the unidirectional inflow feed-pipe of feed-pipe water shoot, and the natural pond liquid being rich in bacterial classification is brought in feed-pipe, utilize the flow direction property of natural pond liquid to promote charging.
6th kind promotes the scheme (hereinafter referred to as the 6th kind of scheme) that natural pond liquid flowing is stirred.
The basis of the 4th kind of scheme is improved, feed-pipe water shoot is provided with the check valve controlling liquid unidirectional inflow feed-pipe in natural pond in water pressure house, the water shoot of cloth bacterium device is provided with the check valve controlling natural pond liquid unidirectional inflow fermentation tube road in water pressure house, the horizontal plane at the lower-most point place of discharge nozzle water shoot is higher than the horizontal plane at feed-pipe water shoot lower-most point place.
When lower-most point lower than the water shoot of cloth bacterium device and water pressure house link position of the horizontal plane at the lower-most point place of discharge nozzle water shoot, in fermentation pipeline, fermentation produces biogas in each fermentation zone inner accumulated, biogas occupies the space in fermentation pipeline, and the natural pond liquid in extruding fermentation pipeline flows in feed-pipe, discharge nozzle, cloth bacterium device, natural pond liquid in fermentation pipeline flows in water pressure house by discharge nozzle water shoot, along with the increase of methane quantity, in fermentation pipeline, natural pond liquid inflow water pressure house is more, and in water pressure house, liquid liquid level in natural pond rises and can reach the water shoot of cloth bacterium device and the link position of water pressure house, when using the biogas stored in any one fermentation zone, biogas air pressure in fermentation pipeline declines, the natural pond liquid stored in water pressure house is made to ferment in pipeline by unidirectional being back to of water shoot of feed-pipe water shoot and cloth bacterium device, and be back in discharge nozzle by discharge nozzle water shoot, when the natural pond liquid liquid level stored in water pressure house is lower than the water shoot of cloth bacterium device and water pressure house link position, the natural pond liquid stored in water pressure house is back in feed-pipe by feed-pipe water shoot is unidirectional and is back in discharge nozzle by discharge nozzle water shoot, when the natural pond liquid liquid level stored in water pressure house continues to decline, when the horizontal plane of the natural pond liquid liquid level stored in water pressure house lower than discharge nozzle water shoot lower-most point place, the natural pond liquid stored in water pressure house can only be back in feed-pipe by feed-pipe water shoot is unidirectional, obviously, the natural pond liquid major part stored in water pressure house is back in feed-pipe by feed-pipe water shoot, and the natural pond liquid being rich in bacterial classification is brought in feed-pipe, utilize the natural pond liquid flowed in feed-pipe, can promote that fermentation raw material flows in fermentation system, thus the dynamic stirring of the natural pond liquid recycle stream completing fermentation system.
When lower-most point higher than the water shoot of cloth bacterium device and water pressure house link position of the horizontal plane at the lower-most point place of discharge nozzle water shoot; Natural pond liquid in fermentation pipeline passes through discharge nozzle water shoot and flows in water pressure house, and along with the biogas air pressure in fermentation pipeline increases, in fermentation pipeline, the amount of natural pond liquid inflow water pressure house is also more; When using the biogas stored in any one fermentation zone, biogas air pressure in fermentation pipeline declines, the natural pond liquid stored in water pressure house is back in fermentation pipeline by the water shoot of feed-pipe water shoot and cloth bacterium device is unidirectional and is back in discharge nozzle by discharge nozzle water shoot, when the natural pond liquid liquid level stored in water pressure house is lower than discharge nozzle water shoot lowest point, the natural pond liquid stored in water pressure house will be fermented in pipeline by feed-pipe water shoot and unidirectional being back to of discharge nozzle water shoot, and what complete natural pond liquid circulates stirring.
7th kind promotes the scheme (hereinafter referred to as the 7th kind of scheme) that natural pond liquid flowing is stirred.
The basis of the 4th kind of scheme is improved, feed-pipe water shoot is provided with the check valve controlling liquid unidirectional inflow feed-pipe in natural pond in water pressure house, discharge nozzle water shoot is provided with the check valve controlling liquid unidirectional inflow water pressure house in natural pond in discharge nozzle, the water shoot of cloth bacterium device is provided with the check valve controlling natural pond liquid unidirectional inflow fermentation tube road in water pressure house.
In fermentation pipeline, fermentation produces biogas in fermentation system inner accumulated, natural pond liquid in extruding fermentation system flows to feed-pipe, discharge nozzle and cloth bacterium device, under the control of check valve, the natural pond liquid being rich in bacterial classification near discharge nozzle can only by the unidirectional inflow water pressure house of discharge nozzle water shoot, and be brought in water pressure house by the natural pond liquid in fermentation pipeline; When using the biogas of fermentation pipeline internal memory storage, in fermentation pipeline, biogas air pressure declines, and the natural pond liquid stored in water pressure house flows in fermentation pipeline respectively by feed-pipe water shoot and by the water shoot of cloth bacterium device is unidirectional, thus completes circulating of natural pond liquid; Circulate in process at natural pond liquid, facilitate being uniformly distributed and promoting that the fermentation raw material near feed-pipe gos deep in fermentation system of bacterial classification, improve the fermentation efficiency of whole fermentation system.
When horizontal plane higher than discharge nozzle water shoot lower-most point place of the horizontal plane at the water shoot of cloth bacterium device and the link position lower-most point place of water pressure house; In the natural pond liquid reflux course stored in water pressure house, when the water shoot lower-most point of the natural pond liquid liquid level stored in water pressure house lower than cloth bacterium device, the natural pond liquid stored in water pressure house can only be back in feed-pipe by feed-pipe water shoot is unidirectional, thus is brought in feed-pipe by the natural pond liquid being rich in bacterial classification.
8th kind promotes the scheme (hereinafter referred to as the 8th kind of scheme) that natural pond liquid flowing is stirred.
The basis of the 4th kind of scheme is improved, feed-pipe water shoot is provided with the check valve controlling liquid unidirectional inflow feed-pipe in natural pond in water pressure house, discharge nozzle water shoot is provided with the check valve controlling liquid unidirectional inflow water pressure house in natural pond in discharge nozzle, the water shoot of cloth bacterium device is provided with the check valve of the unidirectional inflow water pressure house of natural pond liquid controlled in fermentation pipeline, the horizontal plane at the water shoot of cloth bacterium device and the link position lower-most point place of water pressure house is higher than the horizontal plane at discharge nozzle water shoot lower-most point place.
In fermentation pipeline, fermentation produces biogas in fermentation system inner accumulated, natural pond liquid in extruding fermentation system flows to feed-pipe, discharge nozzle and cloth bacterium device, under the control of check valve, natural pond liquid in fermentation pipeline is first by the unidirectional inflow water pressure house of discharge nozzle water shoot, when natural pond liquid liquid level in water pressure house constantly rises and reaches the water shoot extreme lower position of cloth bacterium device, the natural pond liquid in fermentation pipeline is again by the unidirectional inflow water pressure house of water shoot of cloth bacterium device; When using the biogas of fermentation pipeline internal memory storage, biogas air pressure in fermentation pipeline declines, the natural pond liquid stored in water pressure house is by the unidirectional inflow feed-pipe of feed-pipe water shoot, complete circulating of natural pond liquid, the natural pond liquid being rich in bacterial classification to be brought in feed-pipe and the natural pond liquid of flowing promotes that fermentation raw material flows in fermentation system, reach the effect promoting charging.
9th kind promotes the scheme (hereinafter referred to as the 9th kind of scheme) that natural pond liquid flowing is stirred.
The basis of the 4th kind of scheme is improved, feed-pipe water shoot is provided with the check valve controlling liquid unidirectional inflow feed-pipe in natural pond in water pressure house, discharge nozzle water shoot is provided with the check valve controlling liquid unidirectional inflow water pressure house in natural pond in discharge nozzle, the water shoot of cloth bacterium device is provided with the check valve of the unidirectional inflow water pressure house of natural pond liquid controlled in fermentation pipeline, the horizontal plane at the water shoot of cloth bacterium device and the link position lower-most point place of water pressure house is lower than the horizontal plane at discharge nozzle water shoot lower-most point place.
In fermentation pipeline, fermentation produces biogas and in fermentation pipeline inner accumulated, along with the increase of biogas air pressure, natural pond liquid in extruding fermentation pipeline flows in feed-pipe, discharge nozzle and cloth bacterium device, under the control of check valve, natural pond liquid in fermentation pipeline is first by the unidirectional inflow water pressure house of water shoot of cloth bacterium device, when natural pond liquid liquid level in water pressure house reaches the extreme lower position of discharge nozzle water shoot, the natural pond liquid in discharge nozzle is again by the unidirectional inflow water pressure house of discharge nozzle water shoot; When using the biogas of the storage in fermentation pipeline, biogas air pressure in fermentation pipeline declines, the natural pond liquid stored in water pressure house is by the unidirectional inflow feed-pipe of feed-pipe water shoot, complete circulating of natural pond liquid, natural pond liquid in water pressure house is back in feed-pipe process, the natural pond liquid being rich in bacterial classification to be brought in feed-pipe and the natural pond liquid of flowing promotes that fermentation raw material flows in fermentation system, reach the effect promoting charging.
8th kind of scheme compares with the 9th kind of scheme, 8th kind of scheme mainly lays particular emphasis on circulating of natural pond liquid, and the natural pond liquid being rich in bacterial classification is brought in water pressure house, utilize the backflow of natural pond liquid in water pressure house, impel the natural pond liquid being rich in bacterial classification to flow into each position of fermenting in pipeline, improve being uniformly distributed of bacterial classification; 9th kind of scheme mainly lays particular emphasis on the convection agitation of natural pond liquid, first natural pond liquid in fermentation pipeline flow in water pressure house by the cloth tube road of cloth bacterium device, facilitate the natural pond liquid convection agitation in whole fermentation system, utilizing the convection agitation of natural pond liquid, promote being uniformly distributed of bacterial classification, improve the fermentation efficiency of whole fermentation system.
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 (1)

1. the biogas generation systems of assembly type shape of a hoof natural pond liquid sinuous flow produces the method for biogas, and its step comprises:
A, fermentation raw material to be poured in U-shaped fermentation pipeline by feed-pipe and fermentation produces biogas in U-shaped fermentation pipeline, in the space of methane accumulation between feed-pipe sidewall and discharge nozzle sidewall, biogas occupies space in fermentation pipeline and the natural pond liquid that extruding is fermented in pipeline flows in feed-pipe and discharge nozzle, by the unidirectional inflow water pressure house of discharge nozzle water shoot;
B, the biogas using fermentation pipeline internal memory to store up, the biogas air pressure in fermentation pipeline declines, and the natural pond liquid stored is fermented in pipeline by unidirectional being back to of feed-pipe water shoot, complete circulating of natural pond liquid in water pressure house;
C, constantly to produce biogas according to the method for above-mentioned A, B and use biogas, promoting circulating of natural pond liquid.
CN201510030303.2A 2015-01-22 2015-01-22 Biogas generation method for assembly-type U-shaped biogas-slurry-turbulence biogas generation system Withdrawn CN104611198A (en)

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Application publication date: 20150513