CN208933333U - For handling the comb formula dry-process anaerobic fermentation device of stalk - Google Patents
For handling the comb formula dry-process anaerobic fermentation device of stalk Download PDFInfo
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- CN208933333U CN208933333U CN201821341987.3U CN201821341987U CN208933333U CN 208933333 U CN208933333 U CN 208933333U CN 201821341987 U CN201821341987 U CN 201821341987U CN 208933333 U CN208933333 U CN 208933333U
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- 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
Abstract
It is a kind of for handling the comb formula dry-process anaerobic fermentation device of stalk, it include the anaerobic ferment devices ontology with the transfer material front pump (18) for conveying the biogas fermentation material after being inoculated with, it is set as coupling with transfer material front pump (18) and being used to store the inoculation tank (21) of biogas fermentation material, the agitating device for being arranged in inoculation tank (21) and being used to mix storage biogas fermentation material, pass through anaerobic ferment devices ontology, the anaerobic fermentation processing of biogas fermentation material after realizing inoculation, pass through inoculation tank (21) and agitating device, realize that stalk section is mixed with inoculation the uniform of fungus, attachment inoculation is no longer carried out by spray, therefore biogas output rate is improved.
Description
Technical field
The utility model relates to a kind of comb formula dry-process anaerobic fermentation device, especially a kind of comb formula for handling stalk is dry
Method anaerobic ferment devices.
Background technique
The existing processing to stalk is mainly based on burning, returning to the field and wet process anaerobic technology, the burning disposal of stalk, not only
Arable soil structure is destroyed, and the dense smoke generated pollutes air, aggravates haze, seriously affects human health, to friendship
Logical safety constitutes grave danger, and crop straw burning is easy to cause fire incident, and also release carbon dioxide leads to global warming, and returning to the field makes
Soil becomes too loose, and pore size ratio is uneven, macrovoid is excessive, causes to run wind, and soil cannot be in close contact with seed, be influenced
Germination growth, returning to the field amount is excessive or unevenly easily generation edaphon, that is, stover microorganism strives with crop seedling
Take the contradiction of nutrient by force, or even phenomena such as yellow seedling, dead seedling, the underproduction occur, anaerobic fermentation realizes the harmless treatment of biomass, together
When stalk after biogas fermentation, be still good organic fertilizer, be realize circular agriculture a main path, therefore use
In the comb formula dry-process anaerobic fermentation device of processing stalk be a kind of important environmental protecting device, existing for handling the comb of stalk
In formula dry-process anaerobic fermentation device, anaerobic fermentation is divided into dry and wet again, and wet-fermentation needs to consume a large amount of water, and itself
Energy consumption is high, needs to consume 45% or so energy in low temp area, biogas slurry post processing cost is also relatively high, needs very high disposal expense
It is dehydrated, stores, generate a large amount of biogas slurry and do not dissolve, the dry method water consumption about stalk is substantially reduced compared with wet process, almost
There is no sewage discharge, greatly save water rate and sewage disposal expense, biogas slurry of the residues without wet-fermentation, so not having to dehydration
Processing, dry method anaerobic methane quality is high, and sulfur content is far below wet process biogas, can directly use for methane fuelled engine without desulfurization,
The existing dry method anaerobism about stalk is mainly garage type dry method anaerobic technique, this technique does not need any agitating device,
Any input and output material pump is not needed, is inoculated with by spray, although cost very little, inoculum and material are mixed without stirring
It closes, it cannot be guaranteed that inoculum and stalk come into full contact with, so material reaction is insufficient, factor of created gase is low.
Based on applicant's technical problem existing in the Disclosure of invention on July 30th, 2018 and background technique, technology
Feature and technical effect make application technical solution of the invention.
Summary of the invention
The object of the utility model is a kind of for handling the comb formula dry-process anaerobic fermentation device of stalk.
In order to overcome the technical drawbacks described above, the purpose of the utility model is to provide a kind of for handling the comb formula dry method of stalk
Anaerobic ferment devices, therefore improve biogas output rate.
In order to achieve the above objectives, the technical scheme adopted by the utility model is that: include have for convey inoculation after
The anaerobic ferment devices ontology of the transfer material front pump of biogas fermentation material is set as coupling and being used for transfer material front pump
The inoculation tank of biogas fermentation material is stored, is arranged in inoculation tank and is stirred for what is mixed to storage biogas fermentation material
Mix device.
Due to devising anaerobic ferment devices ontology, inoculation tank and agitating device, by anaerobic ferment devices ontology, realize
The anaerobic fermentation of biogas fermentation material after inoculation is handled, and by inoculation tank and agitating device, realizes stalk section and inoculation fungus
Uniform mixing, attachment inoculation is no longer carried out by spray, therefore improves biogas output rate.
The utility model devises, and is used for according to the preposition stalk section of the anaerobic fermentation mode handle mixed with inoculation fungus agitation
The anaerobic ferment devices ontology of main body, inoculation tank used to store are mutually interconnected with the agitating device for generating agitaion power
It connects.
The utility model devises, by such a way that interior closed interval is stirred mixing inoculation tank and agitating device with
The connection of anaerobic ferment devices ontology.
The utility model devises, and anaerobic ferment devices ontology is set as including dry fermentation tank charging supervisor, heating
Coil pipe, discharge nozzle, escape pipe, liquid packing, desulfurizing tower, moisture trap, biogas storage cabinet, material-output tank and anaerobic jar.
The utility model devises, and agitating device is set as including that material absorbs supervisor, material absorbs branch pipe, charging
Pipe, spray branch pipe and major ingredient front pump and material absorb supervisor, material absorption branch pipe, feed pipe, spray branch pipe and major ingredient
Front pump is set as in hydraulic stirring charging distribution.
The utility model devises, also include the first accessories apparatus and the first accessories apparatus setting anaerobic fermentation fill
It sets in ontology, the first accessories apparatus is set as the feed-inputing branched pipe of dry fermentation tank.
The utility model devises, also include the second accessories apparatus and the second accessories apparatus setting anaerobic fermentation fill
It sets between ontology and inoculation tank, the second accessories apparatus is set as including grate plate, outlet pipe and infusion pump.
The utility model devises, and spray branch pipe is provided in inoculation tank and material absorbs branch pipe and sprays branch pipe and sets
It is set to and is connected to by feed pipe with major ingredient front pump, material absorbs branch pipe and is set as absorbing to be responsible for by material being set as and recycling
Pump connection, circulating pump are set as being connected to feed pipe,
Feed-inputing branched pipe, heating coil and the grate plate and dry fermentation tank of dry fermentation tank are respectively arranged in anaerobic jar
Feed-inputing branched pipe be set as by dry fermentation tank feed supervisor and transfer material front pump be inoculated with tank be connected to,
Outlet pipe is arranged on anaerobic jar and anaerobic jar is set as coupling by infusion pump with inoculation tank, discharge nozzle setting
Between anaerobic jar and material-output tank and escape pipe is arranged between anaerobic jar and liquid packing, and liquid packing is set as connecting with desulfurizing tower
Lead to and is provided with moisture trap between biogas storage cabinet and desulfurizing tower.
The utility model devises, and inoculation tank is set as cylindricality tank-like body and sprays the inner cavity that inoculation tank is arranged in branch pipe
The upper end end face portion of body, material absorb branch pipe and the lower end surface portion for the inner chamber body for being inoculated with tank are arranged in and is inoculated with the lower end side of tank
Face is respectively set to the output end oral area of infusion pump, transfer the input terminal oral area of material front pump and material absorption supervisor's connection
It connects, the upper end end face portion for being inoculated with tank is set as coupling with feed pipe.
The utility model devises, and major ingredient front pump is set as the output end oral area of material-handling pump and major ingredient front pump
It is set as coupling with feed pipe, and the input terminal oral area of major ingredient front pump is set as coupling with straw preprocessing pond.
The utility model devises, the input terminal oral area that circulating pump is set as HP jetting pump and circulating pump be set as with
Material absorbs supervisor's connection, and the output end oral area of circulating pump is set as coupling with feed pipe.
The utility model devises, and spray branch pipe is set as including the first branch pipe portion, the second branch pipe portion and third branch pipe
The input terminal oral area of portion and the first branch pipe portion, the input terminal oral area of the second branch pipe portion and the input port part of third branch pipe portion
It is not set as coupling with the output end oral area of feed pipe, the output port of the output end oral area of the first branch pipe portion, the second branch pipe portion
The output end oral area of portion and third branch pipe portion is set as being evenly spaced on and feeding along the circumference of the inner chamber body of inoculation tank
The input terminal oral area of pipe is set as coupling with the output end oral area of major ingredient front pump, feed pipe, the first branch pipe portion, the second branch pipe portion
It is provided in round tubular body respectively with third branch pipe portion and distinguishes in the first branch pipe portion, the second branch pipe portion and third branch pipe portion
It is provided with solenoid valve.
The utility model devises, and material absorbs branch pipe and is set as including the 4th branch pipe portion, the 5th branch pipe portion and the 6th
The output end oral area of branch pipe portion and the 4th branch pipe portion, the output end oral area of the 5th branch pipe portion and the output port of the 6th branch pipe portion
Portion is respectively set to couple with the input terminal oral area of material absorption supervisor, and the output end oral area that material absorbs supervisor is set as and master
The connection of input terminal oral area and material absorption of material front pump are responsible for and are provided in round tubular body, the 4th branch pipe portion, the 5th branch pipe
Portion and the 6th branch pipe portion are respectively set to input loudspeaker port part, the 5th branch pipe portion of tubaeform tubular body and the 4th branch pipe portion
Input loudspeaker port part and the 6th branch pipe portion input loudspeaker port part be set as in upward state be distributed.
The utility model devises, and anaerobic jar is set as cylindricality tank-like body and in the upper end of the inner chamber body of anaerobic jar face
It is provided with the feed-inputing branched pipe of dry fermentation tank, the lower end face of the inner chamber body of anaerobic jar is provided with the upper of grate plate and anaerobic jar
End face portion is respectively set to feed supervisor with dry fermentation tank and escape pipe couples, and the lower end side portion of anaerobic jar is respectively set to
It is provided with heating coil on the inner wall of the inner chamber body of discharge nozzle and outlet pipe and anaerobic jar, is arranged on the outer wall of anaerobic jar
There is the heat preservation rock layer body with a thickness of 15-20cm.
The utility model devises, and the feed-inputing branched pipe of dry fermentation tank is set as including the 7th branch pipe portion, the 8th branch pipe
Portion and the 9th branch pipe portion and the input terminal oral area of the 7th branch pipe portion, the input terminal oral area of the 8th branch pipe portion and the 9th branch pipe portion
The output end oral area that input port portion is respectively set to feed supervisor with dry fermentation tank couples, the output port of the 7th branch pipe portion
The output end oral area in portion, the output end oral area of the 8th branch pipe portion and the 9th branch pipe portion is set as the circumference of the inner chamber body along anaerobic jar
Line is evenly spaced on and the input terminal oral area of dry fermentation tank charging supervisor is set as and transfers the output end for expecting front pump
Oral area connection, the input terminal oral area for transferring material front pump is set as coupling with inoculation tank and the input terminal oral area of discharge nozzle is arranged
It is arranged in material-output tank in the output end oral area of the upper end end face portion of grate plate, discharge nozzle, it is defeated that transfer material front pump is set as material
It send pump and dry fermentation tank feeds supervisor, discharge nozzle, the 7th branch pipe portion, the 8th branch pipe portion and the 9th branch pipe portion and is respectively set to
Round tubular body, material-output tank are set as rectangular storage slot and divide in the 7th branch pipe portion, the 8th branch pipe portion and the 9th branch pipe portion
Solenoid valve is not provided with it.
The utility model devises, and grate plate is provided in round in the center line of plates and grate plate and the vertical of anaerobic jar
Angle between heart line is set as 14-16 °, and the inclination bottom side face of grate plate is set as corresponding with the input terminal oral area of discharge nozzle
It is distributed and is provided with leak hole body in grate plate, the diameter of the leak hole body of grate plate is set as the periphery of 8-12mm and grate plate
Side surface part is set as coupling with anaerobic jar, and the cavity volume between the bottom end end face portion of the inner chamber body of grate plate and anaerobic jar is set as
90-110m3。
The utility model devises, and infusion pump is set as vacuum pump and the input terminal oral area of infusion pump is set as and is discharged
The output end oral area of pipe couples, and the output end oral area of infusion pump is set as and is inoculated with tank and couples and the input terminal oral area of outlet pipe
The lower end surface portion of grate plate is set, and outlet pipe is provided in round tubular body.
The utility model devises, and heating coil is set as steam-heating pipe and heating coil is set as helically line point
Cloth is in anaerobic jar.
The utility model devises, and the input terminal oral area of escape pipe is set as coupling with anaerobic jar and the output of escape pipe
Port part is set as coupling with the input terminal oral area of liquid packing, and the output end oral area of liquid packing is set as through pipeline and desulfurizing tower
The connection of input terminal oral area and the output end oral area of desulfurizing tower be set as the input terminal oral area by pipeline and moisture trap
Connection, the output end oral area of moisture trap are set as coupling by pipeline with biogas storage cabinet, and escape pipe is provided in round pipe
Shape body and liquid packing are set as biogas liquid packing, and desulfurizing tower is set as Marsh gas desulfurizing tower and moisture trap is set as combustion gas
Moisture trap, biogas storage cabinet are set as dry type Double Tops film gas holder.
The utility model devises, and anaerobic jar and inoculation tank, feed pipe, spray branch pipe, material absorption supervisor, material are inhaled
Revenue and expenditure pipe and major ingredient front pump are set as being distributed in such a way that hydrodynamic force mixes and anaerobic jar and grate plate, outlet pipe and infusion
Pump is set as being distributed in the way of extracting effusion.
The charging inoculation tank inoculation temperature that has the technical effect that of the utility model is set as 38 DEG C, 8% < TS < 12%,
It is responsible for by charging, the water suction loudspeaker of the spray charging of feed-inputing branched pipe and the material water suction supervisor of lower end and three water suction branch pipes
Mouth is formed in one and is recycled, and has the function that hydraulic mixing, while solving the easy encrustation phenomena of stalk, stalk and strain are stirred
It mixes and uniformly mixes a certain proportion of cow dung, have adjusted carbon-nitrogen ratio, have facilitation to the starting and subsequent reactions of anaerobism.Three into
Branch pipe 11 is expected by solenoid valve control, and three feed inlets, at 120 ° of angles, can be such that fermentor section covers entirely just around tank body
Lid, is uniformly distributed material, stalk after mixing evenly, is delivered to comb formula anaerobism by feed pipe with feed pump with strain by material
Tank, it is 1000m that tank, which is arranged, in comb formula agitator tank, which holds,3, the stalk of 50t is handled daily, daily charging 10 hours, per hour inlet amount
For 5t, from charging, supervisor enters, and with the feeding manner for being inoculated with tank, point three branch pipes are fed in turn from three different positions, by
Solenoid valve control branch pipe is successively fed 30 minutes in turn, and it is 1cm's that an aperture, which is arranged, in bottom in the comb formula anaerobic jar
Comb formula device, the stalk of processing carries out pretreatment to crush being length 2-3cm, so the size in comb formula device aperture just guarantees straw
Stalk stays in top, and moisture through hole diameter flows to comb formula device in the following, comb formula device level is tilted to the left about 15 ° of angles, favorably
In discharging, discharge nozzle is connected to material-output tank, and material-output tank can keep in biogas residue, and the biogas residue generated does not have to be dehydrated, can be with
Work as organic fertilizer with the mixing of dewatered livestock and poultry biogas residue, 100m is reserved in the lower part of double-edged fine-toothed comb3The space of left and right, goes out in the bottom of anaerobic jar
Water pipe connects a vacuum pump, not only quickly extracts moisture, but also stalk can be compacted, and solid content increases, and passes through
Such operation, realizes dry-type anaerobic fermentation, and the moisture flowed down is connected by the outlet pipe of bottom with inoculation tank, this portion
Point moisture can be used to deploy stalk concentration again, realize recycling for moisture, the surrounding of dry fermentation tank have heating coil with
The heat preservation rock of 15-20cm thickness, the biogas of generation are collected by collection chamber, separate moisture by biogas liquid packing, entrance is subsequent
Desulfurizing and purifying unit is by the H in biogas2S removal continues to remove the remaining moisture in biogas with and by moisture trap, most
The biogas of after-purification is stored by pipeline to gas holder, is inoculated with tank by setting wet type, is stirred stalk and inoculum
Uniformly, it reacts more abundant, improves factor of created gase, the setting of anaerobic jar comb formula device realizes and switchs to dry type by wet type anaerobism and detest
The purpose of oxygen, first biogas residue do not have to be carried out dehydrating, and then anaerobic jar is recycled with tank moisture is inoculated with, saved at
Originally, energy consumption is reduced, no any mechanical stirring device inside anaerobic jar and inoculation tank solves mechanical stirring and is easy to happen event
Barrier, problem not easy to repair reduce costs, and stalk is delivered to anaerobic jar from inoculation tank by feeding pump, solves dry method
The difficult problem of anaerobism charging, easy to operate, the setting of heating coil and heat preservation rock make temperature in tank be kept for 35-38 DEG C, guarantee
The temperature that anaerobism needs, improves factor of created gase, by the invention can by 20% or more the output increased of the biogas of stalk, and
Operating cost is cheap, easy to operate, and controllability is strong, and economy is high, and the feature of environmental protection is significant, and front end is arranged one and connects without churned mechanically
Kind tank, realizes the high-efficiency stirring of material and strain, avoids high, the easy to damage problem of mechanical stirring energy consumption.Comb formula device
Design realizes the dry method anaerobism of material again, not only solves wet process anaerobism energy consumption height, and the high problem of processing cost also solves
Common dry method anaerobism charging is difficult, stirs difficult technical problem.
In the technical scheme, the preposition stalk section of the anaerobic fermentation anaerobic ferment devices sheet mixed with inoculation fungus agitation
Body, inoculation tank and agitating device are important technical characteristic, in the technology of the comb formula dry-process anaerobic fermentation device for handling stalk
In field, there is novelty, creativeness and practicability, term in the technical scheme all can be in the art
Patent document explains and understands.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the schematic diagram of the utility model,
Fig. 2 is the structural schematic diagram of grate plate 4,
Fig. 3 is the distribution schematic diagram of the first branch pipe portion 91, the second branch pipe portion 92 and third branch pipe portion 93,
Dry fermentation tank charging supervisor -1, the feed-inputing branched pipe -2 of dry fermentation tank, heating coil -3, grate plate -4, discharging
Pipe -5, outlet pipe -6, material absorb supervisor -7, material absorb branch pipe -8, escape pipe -9, feed pipe -10, spray branch pipe -11,
Liquid packing -12, moisture trap -14, biogas storage cabinet -15, material-output tank -16, major ingredient front pump -17, turns desulfurizing tower -13
Feeding front pump -18, infusion pump -19, inoculation tank -21, anaerobic jar -22, circulating pump -23, the first branch pipe portion -91, the second branch pipe
Portion -92, third branch pipe portion -93, the 4th branch pipe portion -81, the 5th branch pipe portion -82, the 6th branch pipe portion -83, the 7th branch pipe portion -27,
8th branch pipe portion -28, the 9th branch pipe portion -29.
Specific embodiment
According to guidelines for examination, to such as " having ", "comprising" and " comprising " term should used in the utility model
It is interpreted as not allotting the presence or addition of one or more of the other element or combinations thereof.
It is in the description of the present invention, it should be noted that term " center ", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
For ease of description the utility model and simplify description, rather than the device or element of indication or suggestion meaning must have it is specific
Orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second ", " third " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative 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.
In addition, as long as technical characteristic involved in the utility model different embodiments disclosed below is each other
Not constituting conflict can be combined with each other.
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Fig. 1 is one embodiment of the utility model, illustrates the present embodiment in conjunction with attached drawing, includes dry fermentation
Tank charging supervisor 1, the feed-inputing branched pipe 2 of dry fermentation tank, heating coil 3, grate plate 4, discharge nozzle 5, outlet pipe 6, material absorb master
Pipe 7, material absorb branch pipe 8, escape pipe 9, feed pipe 10, spray branch pipe 11, liquid packing 12, desulfurizing tower 13, gas-water separation
Device 14, material-output tank 16, major ingredient front pump 17, transfers material front pump 18, infusion pump 19, inoculation tank 21, detests biogas storage cabinet 15
Oxygen tank 22 and circulating pump 23,
Inoculation tank 21 in be provided with spray branch pipe 11 and material absorb branch pipe 8 and spray branch pipe 11 be set as by into
Expects pipe 10 is connected to major ingredient front pump 17, and material absorbs branch pipe 8 and is set as being set as and circulating pump 23 by material absorption supervisor 7
Connection, circulating pump 23 are set as being connected to feed pipe 10,
Feed-inputing branched pipe 2, heating coil 3 and the grate plate 4 and dry type of dry fermentation tank are respectively arranged in anaerobic jar 22
The feed-inputing branched pipe 2 of fermentor is set as feeding supervisor 1 by dry fermentation tank and transferring material front pump 18 being connected to inoculation tank 21,
Outlet pipe 6 is arranged on anaerobic jar 22 and anaerobic jar 22 is set as coupling by infusion pump 19 with inoculation tank 21,
Discharge nozzle 5 is arranged between anaerobic jar 22 and material-output tank 16 and escape pipe 9 is arranged between anaerobic jar 22 and liquid packing 12,
Liquid packing 12 is set as that air water point is connected to and be provided between biogas storage cabinet 15 and desulfurizing tower 13 with desulfurizing tower 13
From device 14.
In the present embodiment, inoculation tank 21 be set as cylindricality tank-like body and spray branch pipe 11 be arranged in inoculation tank 21 in
The upper end end face portion of cavity, material absorb branch pipe 8 and the lower end surface portion for the inner chamber body for being inoculated with tank 21 are arranged in and is inoculated with tank 21
Lower end side portion be respectively set to the output end oral area of infusion pump 19, transfer material front pump 18 input terminal oral area and material
7 connection of supervisor is absorbed, the upper end end face portion of inoculation tank 21 is set as coupling with feed pipe 10.
By being inoculated with tank 21, forms and supervisor 7, material absorption branch pipe 8, feed pipe 10 are absorbed to spray branch pipe 11, material
The connection with spray branch pipe 11 is realized, is realized and feed pipe 10 by inoculation tank 21 with the support tie point of infusion pump 19
Connection realizes the connection that branch pipe 8 is absorbed with material, realizes the connection that supervisor 7 is absorbed with material, realizes defeated with transfer material
The connection for entering pump 18, realizes the connection with infusion pump 19, realizes and needs spatial manipulation to stalk inoculation.
In the present embodiment, major ingredient front pump 17 is set as the output end oral area of material-handling pump and major ingredient front pump 17
It is set as coupling with feed pipe 10, and the input terminal oral area of major ingredient front pump 17 is set as coupling with straw preprocessing pond.
By major ingredient front pump 17, form the support tie point to feed pipe 10, by major ingredient front pump 17, realize with
The connection of feed pipe 10 realizes the processing that stalk is conveyed to inoculation tank 21.
In the present embodiment, the input terminal oral area that circulating pump 23 is set as HP jetting pump and circulating pump 23 be set as with
Material absorbs 7 connection of supervisor, and the output end oral area of circulating pump 23 is set as coupling with feed pipe 10.
By circulating pump 23, the support tie point that supervisor 7 is absorbed to feed pipe 10 and material is formd, by circulating pump 23,
The connection with feed pipe 10 is realized, the connection for absorbing supervisor 7 with material is realized, realizes and promotes stalk in inoculation tank 21
The processing of Stirring and broken shell removing dross.
In the present embodiment, spray branch pipe 11 is set as including the first branch pipe portion 91, the second branch pipe portion 92 and third branch
The input terminal oral area of pipe portion 93 and the first branch pipe portion 91, the input terminal oral area of the second branch pipe portion 92 and third branch pipe portion 93 it is defeated
Inbound port portion is respectively set to couple with the output end oral area of feed pipe 10, the output end oral area of the first branch pipe portion 91, second
The output end oral area of pipe portion 92 and the output end oral area of third branch pipe portion 93 are set as the circumference of the inner chamber body along inoculation tank 21
It is evenly spaced on and the input terminal oral area of feed pipe 10 is set as coupling with the output end oral area of major ingredient front pump 17, feed
Pipe 10, the first branch pipe portion 91, the second branch pipe portion 92 and third branch pipe portion 93 are respectively set to round tubular body and at first
Solenoid valve is respectively arranged in pipe portion 91, the second branch pipe portion 92 and third branch pipe portion 93.
By spray branch pipe 11 and feed pipe 10, the support tie point to inoculation tank 21 and major ingredient front pump 17 is formd,
By spray branch pipe 11 and feed pipe 10, the connection with inoculation tank 21 is realized, the connection with major ingredient front pump 17 is realized, by the
One branch pipe portion 91, the second branch pipe portion 92 and third branch pipe portion 93 realize the loading that stalk covers inner chamber body in inoculation tank 21
Processing.
In the present embodiment, material absorbs branch pipe 8 and is set as including the 4th branch pipe portion 81, the 5th branch pipe portion 82 and the 6th
The output end oral area of branch pipe portion 83 and the 4th branch pipe portion 81, the output end oral area of the 5th branch pipe portion 82 and the 6th branch pipe portion 83
The input terminal oral area that output port portion is respectively set to absorb supervisor 7 with material couples, and material absorbs the output end oral area of supervisor 7
It is set as coupling with the input terminal oral area of major ingredient front pump 17 and material absorbs supervisor 7 and is provided in round tubular body, the 4th
Pipe portion 81, the 5th branch pipe portion 82 and the 6th branch pipe portion 83 are respectively set to the input of tubaeform tubular body and the 4th branch pipe portion 81
The input loudspeaker port part of loudspeaker port part, the input loudspeaker port part of the 5th branch pipe portion 82 and the 6th branch pipe portion 83 is set as
It is distributed in upward state.
Branch pipe 8 is absorbed by material and material absorbs supervisor 7, forms the support to inoculation tank 21 and major ingredient front pump 17
Tie point absorbs branch pipe 8 by material and material absorbs supervisor 7, realizes the connection with inoculation tank 21, realizes and input with major ingredient
The connection of pump 17 realizes stalk in inoculation 21 inner cavity of tank by the 4th branch pipe portion 81, the 5th branch pipe portion 82 and the 6th branch pipe portion 83
Rotation processing in body.
In the present embodiment, anaerobic jar 22 is set as cylindricality tank-like body and in the upper end of the inner chamber body of anaerobic jar 22 face
It is provided with the feed-inputing branched pipe 2 of dry fermentation tank, the lower end face of the inner chamber body of anaerobic jar 22 is provided with grate plate 4 and anaerobic jar
22 upper surface portion is respectively set to feed supervisor 1 with dry fermentation tank and escape pipe 9 couples, the lower end side face of anaerobic jar 22
It is respectively set to and is provided with heating coil 3 on the inner wall of the inner chamber body of discharge nozzle 5 and outlet pipe 6 and anaerobic jar 22, detesting
The heat preservation rock layer body with a thickness of 15-20cm is provided on the outer wall of oxygen tank 22.
By anaerobic jar 22, forms and supervisor 1, the feed-inputing branched pipe 2 of dry fermentation tank, heating dish are fed to dry fermentation tank
Pipe 3, grate plate 4, discharge nozzle 5, outlet pipe 6 and escape pipe 9 support tie point realized and dry fermentation tank by anaerobic jar 22
The connection of charging supervisor 1, realizes the connection with the feed-inputing branched pipe 2 of dry fermentation tank, realizes the connection with heating coil 3,
The connection with grate plate 4 is realized, the connection with discharge nozzle 5 is realized, realizes the connection with outlet pipe 6, is realized and outlet
The connection of pipe 9 realizes anaerobic fermentation processing of the stalk in 22 inner chamber body of anaerobic jar.
In the present embodiment, the feed-inputing branched pipe 2 of dry fermentation tank is set as including the 7th branch pipe portion 27, the 8th branch pipe portion
28 and the 9th branch pipe portion 29 and the input terminal oral area of the 7th branch pipe portion 27, the input terminal oral area of the 8th branch pipe portion 28 and the 9th
The output end oral area that the input port portion of pipe portion 29 is respectively set to feed supervisor 1 with dry fermentation tank couples, the 7th branch pipe portion
27 output end oral area, the output end oral area of the 8th branch pipe portion 28 and the output end oral area of the 9th branch pipe portion 29 is set as along anaerobism
The circumference of the inner chamber body of tank 22 is evenly spaced on and the input terminal oral area of dry fermentation tank charging supervisor 1 is set as and is turned
The output end oral area of feeding front pump 18 couples, and the input terminal oral area for transferring material front pump 18 is set as coupling simultaneously with inoculation tank 21
And the upper end end face portion of grate plate 4 is arranged in the input terminal oral area of discharge nozzle 5, the output end oral area of discharge nozzle 5 is arranged in material-output tank
In 16, transfers material front pump 18 and be set as material-handling pump and dry fermentation tank charging supervisor 1, discharge nozzle 5, the 7th branch pipe portion
27, the 8th branch pipe portion 28 and the 9th branch pipe portion 29 are respectively set to round tubular body, and material-output tank 16 is set as rectangular storage slot simultaneously
And solenoid valve is respectively arranged in the 7th branch pipe portion 27, the 8th branch pipe portion 28 and the 9th branch pipe portion 29.
By transferring material front pump 18, dry fermentation tank charging supervisor 1, the feed-inputing branched pipe 2 of dry fermentation tank, discharge nozzle 5
With material-output tank 16, form the support tie point to anaerobic jar 22, by transfer material front pump 18, dry fermentation tank charging supervisor 1,
Feed-inputing branched pipe 2, discharge nozzle 5 and the material-output tank 16 of dry fermentation tank, realize the connection with anaerobic jar 22, expect front pump by transferring
18, the 1, the 7th branch pipe portion 27 of dry fermentation tank charging supervisor, the 8th branch pipe portion 28 and the 9th branch pipe portion 29, realize to anaerobic jar
The loading of 22 inoculation stalk realizes the processing of the discharge to the stalk after anaerobic fermentation by discharge nozzle 5 and material-output tank 16.
In the present embodiment, grate plate 4 is provided in round plates and in the center line of grate plate 4 and the vertical of anaerobic jar 22
Angle between heart line is set as 14-16 °, and the inclination bottom side face of grate plate 4 is set as opposite with the input terminal oral area of discharge nozzle 5
It should be distributed and be provided in grate plate 4 leak hole body, the diameter of the leak hole body of grate plate 4 is set as 8-12mm and grate plate 4
Perimeter sides face be set as coupling with anaerobic jar 22, the chamber between the bottom end end face portion of the inner chamber body of grate plate 4 and anaerobic jar 22
Body volume is set as 90-110m3。
By grate plate 4, the support tie point to anaerobic jar 22 is formd, by grate plate 4, realizes the company with anaerobic jar 22
It connects, realizes the water separating treatment to stalk in anaerobic jar 22.
In the present embodiment, infusion pump 19 is set as vacuum pump and the input terminal oral area of infusion pump 19 is set as and is discharged
The output end oral area of pipe 6 couples, and the output end oral area of infusion pump 19 is set as and is inoculated with tank 21 and couples and the input of outlet pipe 6
The lower end surface portion of grate plate 4 is arranged in port part, and outlet pipe 6 is provided in round tubular body.
By outlet pipe 6 and infusion pump 19, the support tie point to inoculation tank 21 and anaerobic jar 22 is formd, by outlet pipe
6, the connection with anaerobic jar 22 is realized, by infusion pump 19, the connection with inoculation tank 21 is realized, realizes to anaerobic jar 22
It is inoculated with the compaction treatment of stalk.
In the present embodiment, heating coil 3 is set as steam-heating pipe and heating coil 3 is set as helically line distribution
In anaerobic jar 22.
By heating coil 3, the support tie point to anaerobic jar 22 is formd, by heating coil 3, is realized and anaerobic jar
22 connection realizes the isothermal holding to stalk in anaerobic jar 22.
In the present embodiment, the input terminal oral area of escape pipe 9 is set as coupling with anaerobic jar 22 and the output of escape pipe 9
Port part is set as coupling with the input terminal oral area of liquid packing 12, the output end oral area of liquid packing 12 be set as by pipeline with
The input terminal oral area of desulfurizing tower 13 couples and the output end oral area of desulfurizing tower 13 is set as through pipeline and moisture trap
14 input terminal oral area connection, the output end oral area of moisture trap 14 are set as coupling by pipeline with biogas storage cabinet 15,
Escape pipe 9 is provided in round tubular body and liquid packing 12 is set as biogas liquid packing, and desulfurizing tower 13 is set as biogas desulfurization
Tower and moisture trap 14 are set as combustion gas moisture trap, and biogas storage cabinet 15 is set as dry type Double Tops film gas holder.
By escape pipe 9, liquid packing 12, desulfurizing tower 13, moisture trap 14 and biogas storage cabinet 15, form to detesting
The support tie point of oxygen tank 22 realizes the connection with anaerobic jar 22 by escape pipe 9, by liquid packing 12, desulfurizing tower 13, gas
Separator 14 and biogas storage cabinet 15 realize the processing storage of the desulfurization and dehydration to biogas.
In the present embodiment, anaerobic jar 22 and inoculation tank 21, feed pipe 10, spray branch pipe 11, material absorb supervisor 7, object
Material absorbs branch pipe 8 and major ingredient front pump 17 and is set as being distributed in such a way that hydrodynamic force mixes and anaerobic jar 22 and grate plate 4, go out
Water pipe 6 and infusion pump 19 are set as being distributed in the way of extracting effusion.
Stalk is truncated into the stalk section that length is 2-3cm, stalk section, inoculation bacterium and cow dung in straw preprocessing pond
It carries out being mixed to form biogas fermentation material according to weight ratio, starts major ingredient front pump 17, major ingredient front pump 17 is biogas fermentation
Raw material is injected in inoculation tank 21 respectively by the first branch pipe portion 91, the second branch pipe portion 92 and third branch pipe portion 93, is inoculated with simultaneously
Water in tank 21 is received concentration by the 4th branch pipe portion 81, the 5th branch pipe portion 82 and the 6th branch pipe portion 83, is absorbed by material
Supervisor 7 and major ingredient front pump 17 enter in the first branch pipe portion 91, the second branch pipe portion 92 and third branch pipe portion 93, make biogas fermentation
Raw material is in the first branch pipe portion 91, the second branch pipe portion 92 and third branch pipe portion 93 and the 4th branch pipe portion 81, the 5th branch pipe portion 82 and
Hydraulic stirring is carried out between six branch pipe portions 83, stalk section, inoculation bacterium and cow dung are mixed, by the first branch pipe portion 91
The size of open amount of solenoid valve, solenoid valve in the second branch pipe portion 92 open amount size and third branch pipe portion 93 on
The size of the open amount of solenoid valve, the biogas that the biogas fermentation material for spraying the first branch pipe portion 91, the second branch pipe portion 92 are sprayed
The biogas fermentation material that fermentation raw material and third branch pipe portion 93 are sprayed covers on the section of inoculation tank 21, ensure that biogas fermentation
Raw material is uniformly distributed, it is therefore prevented that encrustation phenomena occurs in biogas fermentation material, in inoculation tank 21, completes biogas fermentation material
Uniform inoculation after, starting transfers material front pump 18, and biogas fermentation material after inoculation passes through the 7th branch pipe portion 27, the 8th branch pipe
Portion 28 and the 9th branch pipe portion 29 are injected into anaerobic jar 22, are 1000m when 22 tank of anaerobic jar holds3, the stalk of 50t is handled daily,
Charging 10 hours daily, inlet amount is 5t per hour, passes through the opening and closing of the solenoid valve in the 7th branch pipe portion 27, the 8th branch pipe portion 28
On solenoid valve opening and closing and the 9th branch pipe portion 29 on solenoid valve opening and closing, make the 7th branch pipe portion 27,28 and of the 8th branch pipe portion
9th branch pipe portion 29 is fed in turn from three different positions, is successively fed 30 minutes, is led in turn by solenoid valve control branch pipe
Heating coil 3 is crossed, keeping the internal temperature of anaerobic jar 22 is 35-38 DEG C, and the biogas fermentation material after making inoculation carries out anaerobism hair
Ferment is handled, and the biogas of generation enters liquid packing 12 by escape pipe 9, and biogas carries out desulfurization process by desulfurizing tower 13 and leads to
It crosses after moisture trap 14 carries out gas-liquid separation processing and enters biogas storage cabinet 15 and stored, treated for anaerobic fermentation
Biogas residue passes through the processing of grate plate 4, and the moisture content in biogas residue concentrates on the bottom of the inner chamber body of anaerobic jar 22 by the leak hole body of grate plate 4
Portion is transported to the water in anaerobic jar 22 in inoculation tank 21 by outlet pipe 6 and infusion pump 19, realizes recycling for moisture, combed
The biogas residue being dehydrated on plate 4 is entered in material-output tank 16 by discharge nozzle 5, and the biogas residue of generation does not have to be dehydrated, can be with
Organic fertilizer is worked as in dewatered livestock and poultry biogas residue mixing.
Second embodiment of the utility model, according to the preposition stalk section of the anaerobic fermentation side mixed with inoculation fungus agitation
Formula fills anaerobic ferment devices ontology, inoculation tank 21 used to store and the stirring for generating agitaion power for main body
It sets and is coupled to each other.
The utility model devises, by such a way that interior closed interval is stirred mixing inoculation tank 21 and agitating device
Couple with anaerobic ferment devices ontology.
In the present embodiment, anaerobic ferment devices ontology is set as including 1, heating coil of dry fermentation tank charging supervisor
3, discharge nozzle 5, escape pipe 9, liquid packing 12, desulfurizing tower 13, moisture trap 14, biogas storage cabinet 15, material-output tank 16 and detest
Oxygen tank 22.
In the present embodiment, agitating device is set as including that material absorbs supervisor 7, material absorbs branch pipe 8, feed pipe
10, branch pipe 11 and major ingredient front pump 17 are sprayed and material absorbs supervisor 7, material absorbs branch pipe 8, feed pipe 10, spray branch
Pipe 11 and major ingredient front pump 17 are set as in hydraulic stirring charging distribution.
In the present embodiment, also include the first accessories apparatus and the first accessories apparatus is arranged in anaerobic ferment devices sheet
In body, the first accessories apparatus is set as the feed-inputing branched pipe 2 of dry fermentation tank.
In the present embodiment, also include the second accessories apparatus and the second accessories apparatus is arranged in anaerobic ferment devices sheet
Between body and inoculation tank 21, the second accessories apparatus is set as including grate plate 4, outlet pipe 6 and infusion pump 19.
Second embodiment of the utility model is based on one embodiment.
The utility model has the characteristics that lower:
1, due to devising anaerobic ferment devices ontology, inoculation tank 21 and agitating device, by anaerobic ferment devices ontology,
The anaerobic fermentation processing of biogas fermentation material after realizing inoculation is realized stalk section and is connect by inoculation tank 21 and agitating device
The uniform mixing of kind fungus, no longer carries out attachment inoculation by spray, therefore improve biogas output rate.
2, due to devise dry fermentation tank charging supervisor 1, heating coil 3, discharge nozzle 5, escape pipe 9, liquid packing 12,
Desulfurizing tower 13, moisture trap 14, biogas storage cabinet 15, material-output tank 16 and anaerobic jar 22 realize stalk fermentation and generate natural pond
Gas.
3, supervisor 7 is absorbed due to devising material, material absorbs branch pipe 8, feed pipe 10, spray branch pipe 11 and major ingredient are defeated
Enter pump 17, realize aqueous medium, is stirred mixed feeding.
4, due to devising the feed-inputing branched pipe 2 of dry fermentation tank, the control of the charging to anaerobic jar 22 is realized.
5, due to devising grate plate 4, outlet pipe 6 and infusion pump 19, water circulation and the raw material pressure to anaerobic jar 22 are realized
It is real.
6, the restriction of numberical range has been carried out to planform due to devising, has made the skill of numberical range the utility model
Technical characteristic in art scheme is not to be calculated by formula or test the technical characteristic obtained by limited times, experiments have shown that should
The technical characteristic of numberical range achieves good technical effect.
7, due to devising the technical characteristics of the utility model, in the work of the independent and mutual set of technical characteristic
With, by experiments have shown that, the performance indexes of the utility model is that existing performance indexes is at least 1.7 times, is led to
Crossing assessment has good market value.
There are also other anaerobic ferment devices ontologies mixed with inoculation fungus agitation with the preposition stalk section of anaerobic fermentation, connect
Kind of tank 21 and the technical characteristic of agitating device connection are all one of the embodiments of the present invention, and embodiment described above
Each technical characteristic can be combined arbitrarily, no longer right to meet Patent Law, patent regulation and the requirement of guidelines for examination
The all possible combined embodiment of each technical characteristic in above-described embodiment is all described.
Therefore in the comb formula dry-process anaerobic fermentation device technical field for handling stalk, all includes to have to be used for
The anaerobic ferment devices ontology of the transfer material front pump 18 of biogas fermentation material after conveying inoculation is set as and transfers material input
Pump 18 couples and the inoculation tank 21 for storing biogas fermentation material, setting are in inoculation tank 21 and for storage biogas
The technology contents for the agitating device that fermentation raw material is mixed are all within the protection scope of the present utility model.
Claims (10)
1. it is a kind of for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: including to have for conveying inoculation
The anaerobic ferment devices ontology of the transfer material front pump (18) of biogas fermentation material afterwards is set as and transfers material front pump (18)
Couple and the inoculation tank (21) for storing biogas fermentation material, setting are in inoculation tank (21) and for storage biogas
The agitating device that fermentation raw material is mixed.
2. it is according to claim 1 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: according to anaerobism
Ferment preposition stalk section be inoculated with the mixed mode of fungus agitation the anaerobic ferment devices ontology, used to store for main body
Inoculation tank (21) and the agitating device for generating agitaion power are coupled to each other.
3. it is according to claim 2 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: according to inside
The mode that closed interval is stirred mixing couples inoculation tank (21) and agitating device with anaerobic ferment devices ontology.
4. it is according to claim 1 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: anaerobic fermentation
Device noumenon is set as including dry fermentation tank charging supervisor (1), heating coil (3), discharge nozzle (5), escape pipe (9), water
Device (12), desulfurizing tower (13), moisture trap (14), biogas storage cabinet (15), material-output tank (16) and anaerobic jar (22) are sealed,
Or, agitating device is set as including that material absorbs supervisor (7), material absorbs branch pipe (8), feed pipe (10), spray branch
It manages (11) and major ingredient front pump (17) and material absorbs supervisor (7), material absorbs branch pipe (8), feed pipe (10), spray branch pipe
(11) it is set as with major ingredient front pump (17) in hydraulic stirring charging distribution,
Or, also include that the first accessories apparatus and the first accessories apparatus are arranged in anaerobic ferment devices ontology, the first attachment
Device is set as the feed-inputing branched pipe (2) of dry fermentation tank,
Or, also include the second accessories apparatus and the second accessories apparatus setting anaerobic ferment devices ontology and inoculation tank (21)
Between, the second accessories apparatus is set as including grate plate (4), outlet pipe (6) and infusion pump (19).
5. it is according to claim 4 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: in inoculation tank
(21) it is provided with spray branch pipe (11) in and material absorbs branch pipe (8) and sprays branch pipe (11) and is set as through feed pipe (10)
It is connected to major ingredient front pump (17), material, which absorbs branch pipe (8) and is set as absorbing supervisor (7) by material, to be set as and circulating pump
(23) it being connected to, circulating pump (23) is set as being connected to feed pipe (10),
Be respectively arranged in anaerobic jar (22) feed-inputing branched pipe (2), heating coil (3) and the grate plate (4) of dry fermentation tank and
The feed-inputing branched pipe (2) of dry fermentation tank is set as feeding supervisor (1) by dry fermentation tank and transfers material front pump (18) and connect
Kind tank (21) connection,
Outlet pipe (6) is arranged on anaerobic jar (22) and anaerobic jar (22) is set as through infusion pump (19) and inoculation tank (21)
Connection, discharge nozzle (5) be arranged between anaerobic jar (22) and material-output tank (16) and escape pipe (9) setting in anaerobic jar (22) and
Between liquid packing (12), liquid packing (12) is set as being connected to desulfurizing tower (13) and in biogas storage cabinet (15) and desulfurization
Moisture trap (14) are provided between tower (13).
6. it is according to claim 5 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: inoculation tank
(21) it is set as cylindricality tank-like body and sprays upper end end face portion of branch pipe (11) setting in the inner chamber body of inoculation tank (21), material
Branch pipe (8) setting is absorbed in the lower end surface portion of the inner chamber body of inoculation tank (21) and is inoculated with the lower end side portion difference of tank (21)
It is set as absorbing supervisor (7) with the output end oral area of infusion pump (19), the input terminal oral area of transfer material front pump (18) and material
The upper end end face portion of connection, inoculation tank (21) is set as coupling with feed pipe (10).
7. it is according to claim 5 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: major ingredient inputs
Pump (17) is set as material-handling pump and the output end oral area of major ingredient front pump (17) is set as coupling with feed pipe (10), and
And the input terminal oral area of major ingredient front pump (17) is set as coupling with straw preprocessing pond,
Or, circulating pump (23) is set as HP jetting pump and the input terminal oral area of circulating pump (23) is set as absorbing master with material
(7) connection is managed, the output end oral area of circulating pump (23) is set as coupling with feed pipe (10),
Or, spray branch pipe (11) is set as including the first branch pipe portion (91), the second branch pipe portion (92) and third branch pipe portion (93)
And the input terminal oral area of the first branch pipe portion (91), the input terminal oral area of the second branch pipe portion (92) and third branch pipe portion (93) it is defeated
Inbound port portion is respectively set to couple with the output end oral area of feed pipe (10), the output end oral area of the first branch pipe portion (91),
The output end oral area of two branch pipe portions (92) and the output end oral area of third branch pipe portion (93) are set as along the inner cavity of inoculation tank (21)
The circumference of body is evenly spaced on and the input terminal oral area of feed pipe (10) is set as the output with major ingredient front pump (17)
Port part connection, feed pipe (10), the first branch pipe portion (91), the second branch pipe portion (92) and third branch pipe portion (93) are respectively set to
Round tubular body and electromagnetism is respectively arranged in the first branch pipe portion (91), the second branch pipe portion (92) and third branch pipe portion (93)
Valve,
It is set as including the 4th branch pipe portion (81), the 5th branch pipe portion (82) and the 6th branch pipe portion or, material absorbs branch pipe (8)
(83) and the output end oral area and the 6th branch pipe portion (83) of the output end oral area of the 4th branch pipe portion (81), the 5th branch pipe portion (82)
Output port portion be respectively set to material absorb supervisor (7) input terminal oral area couple, material absorb be responsible for (7) output
Port part is set as coupling with the input terminal oral area of major ingredient front pump (17) and material absorbs supervisor (7) and is provided in round tubulose
Body, the 4th branch pipe portion (81), the 5th branch pipe portion (82) and the 6th branch pipe portion (83) are respectively set to tubaeform tubular body and
The input loudspeaker port part of four branch pipe portions (81), the input loudspeaker port part of the 5th branch pipe portion (82) and the 6th branch pipe portion (83)
Input loudspeaker port part is set as being distributed in upward state.
8. it is according to claim 5 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: anaerobic jar
(22) the upper end face for being set as cylindricality tank-like body and the inner chamber body in anaerobic jar (22) is provided with the charging of dry fermentation tank
Branch pipe (2) is provided with the upper surface part of grate plate (4) and anaerobic jar (22) in the lower end face of the inner chamber body of anaerobic jar (22)
It is not set as feeding supervisor (1) with dry fermentation tank and escape pipe (9) couples, the lower end side portion of anaerobic jar (22) is respectively set
It is provided with heating coil (3) on inner wall for the inner chamber body with discharge nozzle (5) and outlet pipe (6) and anaerobic jar (22), is detesting
The heat preservation rock layer body with a thickness of 15-20cm is provided on the outer wall of oxygen tank (22),
Or, the feed-inputing branched pipe (2) of dry fermentation tank is set as including the 7th branch pipe portion (27), the 8th branch pipe portion (28) and the 9th
The input terminal oral area and the 9th branch pipe of the input terminal oral area of branch pipe portion (29) and the 7th branch pipe portion (27), the 8th branch pipe portion (28)
The output end oral area that the input port portion in portion (29) is respectively set to feed supervisor (1) with dry fermentation tank couples, the 7th branch pipe
The output end oral area of the output end oral area in portion (27), the output end oral area of the 8th branch pipe portion (28) and the 9th branch pipe portion (29) is arranged
For be evenly spaced on along the circumference of the inner chamber body of anaerobic jar (22) and dry fermentation tank charging supervisor (1) input port
Portion is set as coupling with the output end oral area for transferring material front pump (18), and the input terminal oral area for transferring material front pump (18) is set as
With inoculation tank (21) couple and the input terminal oral area of discharge nozzle (5) be arranged grate plate (4) upper end end face portion, discharge nozzle (5)
Output end oral area be arranged in material-output tank (16), transfer material front pump (18) be set as material-handling pump and dry fermentation tank
Charging supervisor (1), discharge nozzle (5), the 7th branch pipe portion (27), the 8th branch pipe portion (28) and the 9th branch pipe portion (29) are respectively set to
Round tubular body, material-output tank (16) are set as rectangular storage slot and in the 7th branch pipe portion (27), the 8th branch pipe portion (28) and
Nine branch pipe portions are respectively arranged with solenoid valve on (29),
Or, heating coil (3) is set as steam-heating pipe and heating coil (3) is set as helically line and is distributed in anaerobic jar
(22) in,
Or, the input terminal oral area of escape pipe (9) is set as coupling with anaerobic jar (22) and the output end oral area of escape pipe (9) is set
It is set to and couples with the input terminal oral area of liquid packing (12), the output end oral area of liquid packing (12) is set as through pipeline and desulfurization
The input terminal oral area of tower (13) couples and the output end oral area of desulfurizing tower (13) is set as through pipeline and moisture trap
(14) input terminal oral area connection, the output end oral area of moisture trap (14) are set as through pipeline and biogas storage cabinet (15)
Connection, escape pipe (9) is provided in round tubular body and liquid packing (12) is set as biogas liquid packing, desulfurizing tower (13) setting
For Marsh gas desulfurizing tower and moisture trap (14) is set as combustion gas moisture trap, and it is double that biogas storage cabinet (15) is set as dry type
Teleblem gas holder.
9. it is according to claim 5 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: grate plate (4)
The angle being provided in round between the center line of plates and grate plate (4) and the vertical centerline of anaerobic jar (22) is set as
14-16 °, the inclination bottom side face of grate plate (4) is set as distribution corresponding with the input terminal oral area of discharge nozzle (5) and in grate plate
(4) leak hole body is provided on, the diameter of the leak hole body of grate plate (4) is set as the peripheral side of 8-12mm and grate plate (4)
Portion is set as coupling with anaerobic jar (22), and the cavity between the bottom end end face portion of the inner chamber body of grate plate (4) and anaerobic jar (22) holds
Product is set as 90-110m3,
Or, infusion pump (19) is set as vacuum pump and the input terminal oral area of infusion pump (19) is set as defeated with outlet pipe (6)
The connection of outlet oral area, the output end oral area of infusion pump (19) are set as and are inoculated with tank (21) and couple and the input of outlet pipe (6)
Port part is arranged in the lower end surface portion of grate plate (4), and outlet pipe (6) is provided in round tubular body.
10. it is according to claim 5 for handling the comb formula dry-process anaerobic fermentation device of stalk, it is characterized in that: anaerobic jar
(22) it is absorbed with inoculation tank (21), feed pipe (10), spray branch pipe (11), material absorption supervisor (7), material branch pipe (8) and main
Material front pump (17) is set as being distributed in such a way that hydrodynamic force mixes and anaerobic jar (22) and grate plate (4), outlet pipe (6) and
Infusion pump (19) is set as being distributed in the way of extracting effusion.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201821341987.3U CN208933333U (en) | 2018-08-20 | 2018-08-20 | For handling the comb formula dry-process anaerobic fermentation device of stalk |
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| CN201821341987.3U CN208933333U (en) | 2018-08-20 | 2018-08-20 | For handling the comb formula dry-process anaerobic fermentation device of stalk |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110452804A (en) * | 2019-07-09 | 2019-11-15 | 上海市政工程设计研究总院（集团）有限公司 | A kind of organic waste dry-type anaerobic digestion device and method |
-
2018
- 2018-08-20 CN CN201821341987.3U patent/CN208933333U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110452804A (en) * | 2019-07-09 | 2019-11-15 | 上海市政工程设计研究总院（集团）有限公司 | A kind of organic waste dry-type anaerobic digestion device and method |
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