CN109401933A - Ruminant-type stalk anaerobic fermentation system and fermentation process - Google Patents
Ruminant-type stalk anaerobic fermentation system and fermentation process Download PDFInfo
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- CN109401933A CN109401933A CN201811571120.1A CN201811571120A CN109401933A CN 109401933 A CN109401933 A CN 109401933A CN 201811571120 A CN201811571120 A CN 201811571120A CN 109401933 A CN109401933 A CN 109401933A
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- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/18—External loop; Means for reintroduction of fermented biomass or liquid percolate
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- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/04—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus by injection or suction, e.g. using pipettes, syringes, needles
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- C12M45/00—Means for pre-treatment of biological substances
- C12M45/02—Means for pre-treatment of biological substances by mechanical forces; Stirring; Trituration; Comminuting
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- C12M45/00—Means for pre-treatment of biological substances
- C12M45/06—Means for pre-treatment of biological substances by chemical means or hydrolysis
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P5/00—Preparation of hydrocarbons or halogenated hydrocarbons
- C12P5/02—Preparation of hydrocarbons or halogenated hydrocarbons acyclic
- C12P5/023—Methane
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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
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Abstract
The present invention provides a kind of ruminant-type stalk anaerobic fermentation systems, including mixing tank and fermentor, the bottom discharge port of the mixing tank is connected to the feed inlet of the fermentor by feed pump, the discharge port of the fermentor is connected to the refluxing opening of the fermentor by circulating pump, and duct type pulverizer is arranged on the pipeline between the circulating pump and the refluxing opening.Meanwhile the present invention also provides ruminant-type stalk anaerobic fermentation methods, complete stalk crushing by feed pump, circulating pump and duct type pulverizer and liquid material stirs, effectively reduce biogas production cost.
Description
Technical field
The present invention relates to biogas project fields, and in particular to a kind of ruminant-type stalk anaerobic fermentation system and fermentation process.
Background technique
In biogas project, in order to obtain high yield gas rate, there must be sufficient contact between bacterium and substrate, usually exist
Thoroughly mixing comprehensively is carried out in fermentor.If mixing is not thorough in fermentor, material meeting in fermentor after a period of time
AUTOMATIC ZONING.In this process, bacterial flora can be assembled in lower level due to its higher density, and the substrate decomposed often compared with
Upper layers of polymer.In this case, contact surface is only limitted to the boundary of two layers of handover, and few degradations occur.Therefore, it is necessary to pass through
Material in stirred fermentor promotes the contact between microorganism and substrate.But excessive mechanical stirring brings larger shear stress
It is easily destroyed the biocoene for producing acetic acid bacteria and methane-producing bacteria, the forming process of biogas is interfered, can also can to anaerobic digestion
It has a negative impact.
In order to solve this problem, in actual operation, it generallys use slow-speed of revolution Stirring device and generates smaller shear stress, keep away
Exempt to destroy bacterium colony, while the material of fermentor thoroughly be stirred after a certain interval, makes material and bacterium can be with
It comes into full contact with, but this scheme operation difficulty is high, is unfavorable for process stabilizing, to influence factor of created gase.
In addition, stalk marsh gas raw materials are not only difficult to mix in threadiness, but also most of energy is all stored in fibre
In dimension, it is difficult to make full use of.Currently, carrying out the grain that physics pretreatment reduction stalk raw materials are mechanically pulverized using stalk crasher
Diameter, and then increase raw material and microorganism contact area, so that raw material is easier to the intrusion and decomposition of microorganism；Original can be also destroyed simultaneously
The crystal structure for expecting hard cell wall and three plain (cellulose, lignin, hemicelluloses), discharges more soluble components
Out, it participates in during biodegrade and methane phase.But it is high microsteping biomass straw class raw material that pretreatment, which is mechanically pulverized,
In biogas utilization one of the step of most expensive, although biogas output, institute can be improved by increasing the specific surface area of raw material
The energy consumption needed is too high.
Summary of the invention
The purpose of the present invention is in view of the deficiencies of the prior art, thus provide a kind of ruminant-type stalk anaerobic fermentation system and
Fermentation process.
To achieve the goals above, the technical scheme adopted by the invention is that:
A kind of ruminant-type stalk anaerobic fermentation system, including mixing tank and fermentor, the bottom discharge port of the mixing tank pass through
Feed pump is connected to the feed inlet of the fermentor, and the discharge port of the fermentor is connected to the reflux of the fermentor by circulating pump
Mouthful, duct type pulverizer is set on the pipeline between the circulating pump and the refluxing opening.
Based on above-mentioned, at least two feed inlets and at least two refluxing openings are arranged in the side wall of the fermentor,
Each feed inlet and the refluxing opening are uniformly distributed on a certain circumference of the fermentation pot sidewall, the outflow of the feed pump
End is separately connected each feed inlet, and the outflux of the duct type pulverizer is separately connected each refluxing opening.
Based on above-mentioned, the discharge port is located above the refluxing opening.
Based on above-mentioned, setting branch refluxing opening, the outflow end of the circulating pump between the discharge port and the refluxing opening
It is also connected with the branch refluxing opening.
Based on above-mentioned, which further includes feeding vehicle, batch meter and stalk conveyer belt, institute
It states batch meter, the stalk conveyer belt and the mixing tank and is respectively positioned on underground, so that stalk passes through after batch meter metering
The stalk conveyer belt enters the mixing tank, and the fermentor is located at ground.
Based on above-mentioned, the side of the duct type pulverizer is equipped with fast-open type services aperture.
A method of ruminant-type stalk anaerobic fermentation is carried out using the system comprising following steps:
Stalk and biogas slurry are sufficiently mixed in mixing tank, obtain mixed material；
The mixed material is delivered in fermentor by feed pump, stands 1 ~ 30 day, obtains softening material；
The softening material is flowed out from the discharge port of the fermentor, then the refluxing opening of the fermentor is flowed to by circulating pump,
Circulation 5 ~ 50 hours.
Based on above-mentioned, at least two feed inlets and at least two refluxing openings are arranged in the side wall of the fermentor,
Each feed inlet and the refluxing opening are uniformly distributed on a certain circumference of the fermentation pot sidewall；The mixing tank and each institute
It states feed inlet circulation connection to be fed, each feed inlet is connected to 1 ~ 10 hour；The discharge port of the fermentor and each institute
It states refluxing opening circulation connection and carries out Matter Transfer, each refluxing opening is connected to 1 ~ 10 hour.
Based on above-mentioned, setting branch refluxing opening, the outflow end of the circulating pump between the discharge port and the refluxing opening
It is also connected with the branch refluxing opening；The discharge port of the fermentor be connected to each refluxing opening circulation progress Matter Transfer it
Before, the circulating pump is connected to the branch refluxing opening first, is stirred 1 ~ 24 hour in advance.
The present invention has substantive distinguishing features outstanding and marked improvement compared with the prior art, specifically, the present invention has
Following advantages:
Ruminant-type stalk anaerobic fermentation system provided by the invention is by conventional disperse, the hydrolysis of isolation, crushing, agitating procedure to send out
Fermentation tank is carrier organic integration, realizes multi-functional linkage, production cost is lower, and operational efficiency is higher.Specifically, stalk and natural pond
After liquid mixes in mixing tank, stalk is cut by the rotary blade in feed pump, circulating pump, then passes through duct type
Pulverizer is crushed, so that stalk carries out biodegrade, has both met biogas production demand, without expensive high-power stalk
Dedicated grinding device greatly reduces the cost that stalk anaerobic fermentation prepares biogas；Material is carried out by circulating pump simultaneously to follow
Ring, in fermentor material carry out hydraulic mixing, compared with mechanical stirring, hydraulic mixing is milder, will not moment to hair
Material generates strong disturbance in fermentation tank, is conducive to the relatively stable of bacterial flora distributional pattern；Further, refluxing opening is distributed in fermentation
The different location of tank, and successively running ensure that the slow super distributed of bacterial flora of lower layer's deposition is spread upwardly, meet material with
The contact demand of bacterial flora.
Meanwhile the present invention also provides ruminant-type stalk anaerobic fermentation method, stalk and biogas slurry are first mixed, are then passed through
Feed pump is delivered in fermentor, in feed pump carry out first time cutting, into fermentor after first carry out standing softening, stalk
Static immersing process can also be completed to hydrolyze in fermentor, without in addition configuration hydrolytic decomposition pot or hydrolytic tank, simplify production work
Sequence, while static softening can soften the hard fibre of stalk, be also beneficial to it is subsequent further stalk is cut and is crushed,
Reduce Grin-ding energ7 and enhancing crushing effect.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of ruminant-type stalk anaerobic fermentation system in the present invention.
Fig. 2 is the feed inlet of the fermentor and the distribution schematic diagram of refluxing opening.
Fig. 3 is the structural schematic diagram of the duct type pulverizer.
In figure: 1. feeding vehicles；2. batch meter；3. stalk conveyer belt；4. mixing tank；5. feed pump；6. fermentor；
7. circulating pump；8. duct type pulverizer；9. branch refluxing opening；10. refluxing opening；11. main road valve；12. branch road valve；
13. feed inlet；14. discharge port；15. fast-open type services aperture.
Specific embodiment
Below by specific embodiment, technical scheme of the present invention will be described in further detail.
As shown in Figure 1-3, a kind of ruminant-type stalk anaerobic fermentation system, including mixing tank 4 and fermentor 6, the mixing
The bottom discharge port of tank 6 is connected to the feed inlet 13 of the fermentor 6 by feed pump 5, and the discharge port of the fermentor 6 is by following
Ring pump 7 is connected to the refluxing opening of the fermentor 6, and duct type is arranged on the pipeline between the circulating pump 7 and the refluxing opening 10
Pulverizer.In the present embodiment, the power of the duct type pulverizer is 1.1 kW, can be selected as needed in other examples
The duct type pulverizer for being 0.5 ~ 50 kW with power, preferably power are the duct type pulverizer of 1.1 ~ 5.5 kW.
It is a kind of to carry out ruminant-type stalk anaerobic fermentation method using the ruminant-type stalk anaerobic fermentation system comprising with
Lower step:
Stalk and biogas slurry are sufficiently mixed in mixing tank 4, incorporation time is 5 ~ 100 minutes, obtains mixed material；According to
The ratio of stalk and biogas slurry, the specification of mixing tank adjust incorporation time, it is preferred that the incorporation time is 10 ~ 30 minutes；
The mixed material is delivered in fermentor by feed pump, stands 1 ~ 30 day, obtains softening material；Feed pump plays defeated
It send material and cuts the effect of stalk, stand process stalk and obtain impregnating softening, can not only soften the hard fibre of stalk, drop
Low Grin-ding energ7 and enhancing crushing effect, convenient for being crushed subsequently through circulating pump cutting and pipes crasher, without expensive big
The dedicated grinding device of power stalk greatly reduces the cost that stalk anaerobic fermentation prepares biogas；Meanwhile standing process is also
The process of reaction is hydrolyzed, specifically, time of repose can be selected according to stalk and the case where biogas slurry, it is preferred that stand
Time is 3 ~ 7 days；
The softening material is constantly flowed out from the discharge port of the fermentor, then the reflux of the fermentor is flowed to by circulating pump
Mouthful, by circulation 5 ~ 50 hours, completes stalk Total continuity and crush and the full hydraulic mixing of fermentor material.Compared with mechanical stirring,
Hydraulic mixing is milder, moment will not generate strong disturbance to material in fermentor, be conducive to the phase of bacterial flora distributional pattern
To stabilization, fermentation efficiency is improved.
Further, at least two feed inlets 13 and at least two refluxing openings are arranged in the side wall of the fermentor 6
10, each feed inlet 13 and the refluxing opening 10 are uniformly distributed on a certain circumference of 6 side wall of fermentor, the charging
The outflow end of pump 5 is separately connected each feed inlet 13, and the outflux of the duct type pulverizer 8 is separately connected each reflux
Mouth 10.
The fermentor 6 when being fed each feed inlet be sequentially communicated, so as to the different location of fermentor 6 carry out into
Material, plays certain mixing effect；It completes to stand step after charging, when being flowed back in the fermentor 6 by circulating pump 7,
The outflux of the duct type pulverizer 8 is sequentially communicated with each refluxing opening 10 respectively, to be returned in different positions
Stream, it is more uniform to stir and to crush, avoid only carrying out hydraulic mixing in point, be unable to fully be stirred and powder
It is broken.The number and distribution of feed inlet 13 and refluxing opening 10 can be adjusted according to the specification of fermentor 6, in the present embodiment, such as Fig. 2
Shown, 10-1 ~ 10-5 is refluxing opening, and 13-1 ~ 13-3 is feed inlet, and feed pump 5 is delivered to feed inlet 13-1 and enters hair when charging
Fermentation tank 6, the process continue 1 ~ 10 hour, then switch to feed inlet 13-2, and material enters fermentor 6 by feed inlet 13-2, should
Process also continues 1 ~ 10 hour, is finally switched to feed inlet 13-3, and material enters fermentor 6 by feed inlet 13-3, the process
Continue 1 ~ 10 hour；Then it is switched to feed inlet 13-1 circulate operation again until charging finishes；Preferably, the charging of each feed inlet
Time is 1 ~ 3 hour；When reflux, material returns in fermentor from refluxing opening 10-1, which continues 1 ~ 10 hour, then switches
To refluxing opening 10-2, material returns to fermentor 6 by refluxing opening 10-2, which also continues 1 ~ 10 hour, then switch to reflux
Mouth 10-3, material return to fermentor 6 by refluxing opening 10-3, which also continues 1 ~ 10 hour, then switch to refluxing opening 10-4,
Material returns to fermentor 6 by refluxing opening 10-4, which also continues 1 ~ 10 hour, is finally switched to refluxing opening 10-5, material by
Refluxing opening 10-5 returns to fermentor 6, which also continues 1 ~ 10 hour, and so far stalk Total continuity crushes and the full water of fermentor material
Power stirring is completed.Preferably, the return time of each refluxing opening is 1 ~ 3 hour.
Further, in order to reduce conveying energy consumption by gravity, the discharge port 14 is located at 10 top of refluxing opening.
Further, branch refluxing opening 9, the stream of the circulating pump 7 are set between the discharge port 14 and the refluxing opening 10
Outlet is also connected with the branch refluxing opening 9.So that before carrying out reflux hydraulic mixing, the outflow end of the circulating pump 7 is connected to
The branch refluxing opening 9 is opened branch road valve 12 and is stirred in advance, and pre- mixing time is 1 ~ 24 hour, is then shut off bypass valve
Door 12 opens main road valve 11, carries out hydraulic mixing；Preferably, pre- mixing time is 3 ~ 5 hours.
Further, the ruminant-type stalk anaerobic fermentation system, further includes feeding vehicle 1, batch meter 2 and stalk conveyer belt 3, with
Just stalk enters the mixing tank by the stalk conveyer belt 3 after the batch meter 2 metering.Material is introduced into meter when charging
Measuring tank 2, if batch meter 2 is put it on the ground, feeding vehicle 1 needs longer arm exhibition, the batch meter 2, described in order to feed conveniently
Stalk conveyer belt 3 and the mixing tank are respectively positioned on underground, and the fermentor is located at ground.
Further, the side of the duct type pulverizer 8 is equipped with fast-open type services aperture 15 and avoids straw periodically to clear up
Stalk blocking.
Finally it should be noted that: the above embodiments are merely illustrative of the technical scheme of the present invention and are not intended to be limiting thereof；To the greatest extent
The present invention is described in detail with reference to preferred embodiments for pipe, it should be understood by those ordinary skilled in the art that: still
It can modify to a specific embodiment of the invention or some technical features can be equivalently replaced；Without departing from this hair
The spirit of bright technical solution should all cover within the scope of the technical scheme claimed by the invention.
Claims (9)
1. a kind of ruminant-type stalk anaerobic fermentation system, it is characterised in that: including mixing tank and fermentor, the bottom of the mixing tank
Portion's discharge port is connected to the feed inlet of the fermentor by feed pump, and the discharge port of the fermentor passes through described in circulating pump connection
Duct type pulverizer is arranged on the pipeline between the circulating pump and the refluxing opening for the refluxing opening of fermentor.
2. ruminant-type stalk anaerobic fermentation system according to claim 1, it is characterised in that: the side wall of the fermentor is set
At least two feed inlets and at least two refluxing openings are set, each feed inlet and the refluxing opening are uniformly distributed in institute
On a certain circumference for stating fermentation pot sidewall, the outflow end of the feed pump is separately connected each feed inlet, the duct type powder
The outflux of broken machine is separately connected each refluxing opening.
3. ruminant-type stalk anaerobic fermentation system according to claim 1 or 2, it is characterised in that: the discharge port is located at
Above the refluxing opening.
4. ruminant-type stalk anaerobic fermentation system according to claim 3, it is characterised in that: the discharge port and described time
Branch refluxing opening is set between head piece, and the outflow end of the circulating pump is also connected with the branch refluxing opening.
5. ruminant-type stalk anaerobic fermentation system according to claim 4, it is characterised in that: further include feeding vehicle, metering
Case and stalk conveyer belt, the batch meter, the stalk conveyer belt and the mixing tank are respectively positioned on underground, so that stalk is described
The mixing tank is entered by the stalk conveyer belt after batch meter metering, the fermentor is located at ground.
6. ruminant-type stalk anaerobic fermentation system according to claim 4 or 5, it is characterised in that: the duct type crushes
The side of machine is equipped with fast-open type services aperture.
7. a kind of method for carrying out ruminant-type stalk anaerobic fermentation using system described in any one of claims 1-6 comprising
Following steps:
Stalk and biogas slurry are sufficiently mixed in mixing tank, obtain mixed material；
The mixed material is delivered in fermentor by feed pump, stands 1 ~ 30 day, obtains softening material；
The softening material is flowed out from the discharge port of the fermentor, then the refluxing opening of the fermentor is flowed to by circulating pump,
Circulation 5 ~ 50 hours is completed stalk Total continuity and is crushed and the full hydraulic mixing of fermentor material.
8. ruminant-type stalk anaerobic fermentation method according to claim 7, it is characterised in that: the side wall of the fermentor is set
At least two feed inlets and at least two refluxing openings are set, each feed inlet and the refluxing opening are uniformly distributed in institute
On a certain circumference for stating fermentation pot sidewall；The mixing tank and each feed inlet are sequentially communicated and are fed, it is each described into
Material mouth is connected to 1 ~ 10 hour；The discharge port of the fermentor and each refluxing opening are sequentially communicated carry out Matter Transfer, Mei Gesuo
Refluxing opening is stated to be connected to 1 ~ 10 hour.
9. ruminant-type stalk anaerobic fermentation method according to claim 8, it is characterised in that: the discharge port and described time
Branch refluxing opening is set between head piece, and the outflow end of the circulating pump is also connected with the branch refluxing opening；In the fermentor
Discharge port and each refluxing opening are sequentially communicated before carrying out Matter Transfer, first connect the circulating pump and the branch refluxing opening
It is logical, it stirs 1 ~ 24 hour in advance.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201811571120.1A CN109401933A (en) | 2018-12-21 | 2018-12-21 | Ruminant-type stalk anaerobic fermentation system and fermentation process |
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| CN201811571120.1A CN109401933A (en) | 2018-12-21 | 2018-12-21 | Ruminant-type stalk anaerobic fermentation system and fermentation process |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110295105A (en) * | 2019-08-07 | 2019-10-01 | 任进礼 | Duct type slaking apparatus, methane producing system and methane producing method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010009668A1 (en) * | 2008-07-21 | 2010-01-28 | 胜利油田胜利动力机械集团有限公司 | Straw fermentation process and device thereof |
| CN104404087A (en) * | 2014-11-27 | 2015-03-11 | 辽宁省能源研究所 | Technological method for preparing biogas by utilizing high-concentration organic waste and fermentation system thereof |
| CN105199942A (en) * | 2015-08-25 | 2015-12-30 | 桑德环境资源股份有限公司 | Resourceful and harmless treatment system for organic waste in villages and towns and method thereof |
| CN106497759A (en) * | 2016-11-30 | 2017-03-15 | 上海市政工程设计研究总院（集团）有限公司 | A kind of anaerobic jar scum silica frost EGR |
| CN209493572U (en) * | 2018-12-21 | 2019-10-15 | 河南恒天久大实业有限公司 | Ruminant-type stalk anaerobic fermentation system |
-
2018
- 2018-12-21 CN CN201811571120.1A patent/CN109401933A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010009668A1 (en) * | 2008-07-21 | 2010-01-28 | 胜利油田胜利动力机械集团有限公司 | Straw fermentation process and device thereof |
| CN104404087A (en) * | 2014-11-27 | 2015-03-11 | 辽宁省能源研究所 | Technological method for preparing biogas by utilizing high-concentration organic waste and fermentation system thereof |
| CN105199942A (en) * | 2015-08-25 | 2015-12-30 | 桑德环境资源股份有限公司 | Resourceful and harmless treatment system for organic waste in villages and towns and method thereof |
| CN106497759A (en) * | 2016-11-30 | 2017-03-15 | 上海市政工程设计研究总院（集团）有限公司 | A kind of anaerobic jar scum silica frost EGR |
| CN209493572U (en) * | 2018-12-21 | 2019-10-15 | 河南恒天久大实业有限公司 | Ruminant-type stalk anaerobic fermentation system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110295105A (en) * | 2019-08-07 | 2019-10-01 | 任进礼 | Duct type slaking apparatus, methane producing system and methane producing method |
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