CN204125315U - A kind of plant biogas fermentation device - Google Patents
A kind of plant biogas fermentation device Download PDFInfo
- Publication number
- CN204125315U CN204125315U CN201420587251.XU CN201420587251U CN204125315U CN 204125315 U CN204125315 U CN 204125315U CN 201420587251 U CN201420587251 U CN 201420587251U CN 204125315 U CN204125315 U CN 204125315U
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- pond
- density
- raw materials
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- materials pretreatment
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- 238000000855 fermentation Methods 0.000 title claims abstract description 23
- 230000004151 fermentation Effects 0.000 title claims abstract description 22
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 27
- 239000002994 raw material Substances 0.000 claims abstract description 15
- 241000196324 Embryophyta Species 0.000 claims abstract description 10
- 239000002244 precipitate Substances 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 claims abstract description 8
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims abstract description 4
- 235000017491 Bambusa tulda Nutrition 0.000 claims abstract description 4
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims abstract description 4
- 239000011425 bamboo Substances 0.000 claims abstract description 4
- 239000004033 plastic Substances 0.000 claims abstract description 4
- 229920003023 plastic Polymers 0.000 claims abstract description 4
- 240000003917 Bambusa tulda Species 0.000 claims abstract 2
- 238000003860 storage Methods 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 12
- 241000282898 Sus scrofa Species 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 5
- 230000002349 favourable Effects 0.000 claims description 3
- 230000005484 gravity Effects 0.000 claims description 3
- 239000007787 solid Substances 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 abstract description 4
- 238000009826 distribution Methods 0.000 abstract description 2
- 238000004062 sedimentation Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 description 4
- 241001330002 Bambuseae Species 0.000 description 2
- 210000003608 Feces Anatomy 0.000 description 2
- 230000031018 biological processes and functions Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000010871 livestock manure Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 241000282887 Suidae Species 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 230000001488 breeding Effects 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000000384 rearing Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
The utility model provides a kind of plant biogas fermentation device, belongs to and relates to plant's apparatus field, and this device comprises raw materials pretreatment mechanism and anaerobically fermenting mechanism; Described raw materials pretreatment mechanism is solid-liquid separator, be divided into flash trapping stage device and secondary separation device, wherein flash trapping stage device is woven plastics filter screen or bamboo sieve plate, secondary separation device is two-stage precipitate and separate groove, the density pond that this precipitate and separate groove is not waited by two volumes is formed by connecting, can twice deposition be carried out, improve the sedimentation effect of solid matter and the efficiency of subsequent solid mass treatment; Described anaerobically fermenting mechanism is methane-generating pit, adopts many ponds to combine, can effective water distribution and to dam pollution, bears greater impact load, ensure that piggery wastewater is able to efficient process.
Description
Technical field
The utility model relates to plant's apparatus field, is specifically related to utilize the biogas fermentation device of ight soil of raising pigs.
Background technology
Industrialized culture has become the inevitable development trend that domestic and international live pig produces, China's development in recent years rapidly and scale constantly expand.This mode of production is conducive to improving the breeding technology on pig farm, epidemic prevention level, food utilization efficiency and level of management, greatly reduces production cost than traditional peasant household dispersion raising and boosts productivity.Meanwhile, this batch production is concentrated and is raised live pig, also makes animal manure and Waste Water Centralized, poses a big pressure to environment, as not scientific and normal process, is bound to serious environment pollution and water source, also affect the normal production of live pig self.This problem has become one of focus be concerned about in this field both at home and abroad.But the intractability of piggery wastewater is very large, and one is water displacement; Two is that solid-liquid mixes, and organic concentration is higher; Three is that pig-breeding industry belongs to the lower industry of profit, is also subject to the dual-pressure in nature and market simultaneously.Therefore, only have the animal manure wastewater treatment equipment that less investment, running cost are low, convenient management, treatment effect are good and the zymotechnique matched, can promote the use of in industrialized culture industry, after making wastewater treatment, be able to recycling, both decontamination, turns harm into good again.
At present, the best method of pig farm offal treatment adopts biological processes, in biological processes process, needs through anaerobically fermenting, and in anaerobic fermentation process, organic substance decomposing produces the materials such as biogas and nitrogenous, phosphorus.Biogas is fabulous energy substance, and its calorific value is higher, only produces carbonic acid gas and water after burning.If the output of biogas is sufficient in pig farm, just as the energy of generating, therefore can save massive diesel-fuel, this lacks solution China energy, changes rural area looks, improves life of farmers quality and be of great importance.
Summary of the invention
The utility model aims to provide a kind of plant biogas fermentation device, this apparatus structure is easy, cost is low, floor space is little, fermenting power is strong, safe and reliable to operation, long service life, realize processing the waste produced in swine rearing process, use it for production biogas, while reducing environmental pollution, save traditional energy.
For achieving the above object, the utility model by the following technical solutions: a kind of plant biogas fermentation device, comprises raw materials pretreatment mechanism and anaerobically fermenting mechanism;
Described raw materials pretreatment mechanism is solid-liquid separator, comprise flash trapping stage device 1 and secondary separation device, wherein flash trapping stage device 1 is woven plastics filter screen or bamboo sieve plate, and it is arranged between pig house and fermentation unit, from height to low setting, favourable physical features is utilized to carry out raw material gravity flow; Described secondary separation device is two-stage precipitate and separate groove, the density pond that this precipitate and separate groove is not waited by two volumes is formed by connecting, No. two density pond 3 volumes are 2 to 3 times of density pond 2 volume, pipe material 4 is all set out bottom a density pond 2 and No. two density ponds 3, and be equipped with a square breach 5 above side, to realize the flowing of solidliquid mixture; Arrange breach between a density pond 2 and No. two density ponds 3 to enter No. two density ponds 3 by the post-depositional solidliquid mixture of one-level and carry out secondary deposition; Liquid after secondary deposition is discharged by No. two density pond 3 opposite side setting party v notch vs 5;
Described anaerobically fermenting mechanism is methane-generating pit, be arranged on raw materials pretreatment mechanism lower end, it adopts domes, be two skene arch compositions up and down, comprise more than 2 and pond of itemizing, each single pond comprises fermentation vat 6, feed-pipe 7, natural pond liquid storage pool 8, liquid discharge pipe 9 and airway 10, airway 10 is communicated with gas storage holder 11 with fermentation vat 6, described gas storage holder 11 is provided with two, each single pond gas storage holder 11 is collected to large gas-holder, the natural pond liquid storage pool 8 in each single pond is pooled to natural pond liquid hold tank, is provided with liquid discharge pipe 9.
Stirrer can be provided with at described Dan Chi top, improve attenuation degree.
Two-stage precipitate and separate groove in the utility model raw materials pretreatment mechanism effectively can improve the sedimentation effect of solid matter in solidliquid mixture, and described density pond provides two solid matter output channels simultaneously, improves the efficiency of subsequent solid mass treatment; This biogas fermentation device is rational in infrastructure, stress performance good, weather resistance is strong; This device adopts many ponds to combine, can effective water distribution and to dam pollution, bears greater impact load, ensure that piggery wastewater is able to efficient process; This device is suited measures to local conditions, laid down cost is low, construction period is short, go into operation then and take effect, good sewage processing effect, rear utilization is reasonable, become large-scale " pig-natural pond-really " development mode of pig farm, biogas engineering and garden spot, economy and environment benefit is very remarkable, and results form investment level is high, achieves the lower cost under equal index.
Accompanying drawing explanation
Fig. 1 is the structural representation of described plant biogas fermentation device;
Fig. 2 is described two-stage precipitate and separate groove structural representation;
Fig. 3 is the internal structure schematic diagram in described single pond;
In figure, density pond 3, flash trapping stage device No. 2, two, 1, density pond, discharge pipe 4, square breach 5, fermentation vat 6, feed-pipe 7, natural pond liquid storage pool 8, liquid discharge pipe 9, airway 10, gas storage holder 11.
Embodiment
Below in conjunction with accompanying drawing and explanation, the present invention is further described.
embodiment 1
As shown in Figure 1, 2, 3, a kind of plant biogas fermentation device described in the present embodiment, comprises raw materials pretreatment mechanism and anaerobically fermenting mechanism; Described raw materials pretreatment mechanism is solid-liquid separator, comprise flash trapping stage device 1 and secondary separation device, wherein flash trapping stage device 1 is woven plastics filter screen or bamboo sieve plate, and it is arranged between pig house and fermentation unit, from height to low setting, favourable physical features is utilized to carry out raw material gravity flow; Described secondary separation device is two-stage precipitate and separate groove, the density pond that this precipitate and separate groove is not waited by two volumes is formed by connecting, No. two density pond 3 volumes are 2 to 3 times of density pond 2 volume, pipe material 4 is all set out bottom a density pond 2 and No. two density ponds 3, and be equipped with a square breach 5 above side, to realize the flowing of solidliquid mixture; Arrange breach between a density pond 2 and No. two density ponds 3 to enter No. two density ponds 3 by the post-depositional solidliquid mixture of one-level and carry out secondary deposition; Liquid after secondary deposition is discharged by No. two density pond 3 opposite side setting party v notch vs 5; Described anaerobically fermenting mechanism is methane-generating pit, be arranged on raw materials pretreatment mechanism lower end, it adopts domes, be two skene arch compositions up and down, comprise more than 2 and pond of itemizing, each single pond comprises fermentation vat 6, feed-pipe 7, natural pond liquid storage pool 8, liquid discharge pipe 9 and airway 10, airway 10 is communicated with gas storage holder 11 with fermentation vat 6, described gas storage holder 11 is provided with two, each single pond gas storage holder 11 is collected to large gas-holder, the natural pond liquid storage pool 8 in each single pond is pooled to natural pond liquid hold tank, is provided with liquid discharge pipe 9.
During the work of this device, carry out according to following flow process: first the solidliquid mixture after flash trapping stage device 1 is separated enters a less density pond 2 of volume, because the density of solid matter is higher than the density of liquid, solid matter will deposit in a density pond 2 greatly.Meanwhile, because the volume restriction in hydraulic shock and density pond makes a part of solid matter can not deposit in a density pond 2, the liquid in a density pond 2 can be suspended at the middle and upper levels.And automatically can enter No. two density ponds 3 by the square breach 5 in side, a density pond 2 after the solid matter on upper strata to certain altitude, the mixture recovery be actually a density pond 2 processed deposits again.The volume that No. two density ponds 3 are larger and less mobility make solid matter obtain enough depositing times and space, the solid matter do not deposited in a density pond 2 is fully deposited, improves the quality of biogas fermentation material.
Claims (2)
1. plant's biogas fermentation device, is characterized in that, comprises raw materials pretreatment mechanism and anaerobically fermenting mechanism;
Described raw materials pretreatment mechanism is solid-liquid separator, comprise flash trapping stage device (1) and secondary separation device, wherein flash trapping stage device (1) is woven plastics filter screen or bamboo sieve plate, it is arranged between pig house and fermentation unit, from height to low setting, favourable physical features is utilized to carry out raw material gravity flow; Described secondary separation device is two-stage precipitate and separate groove, the density pond that this precipitate and separate groove is not waited by two volumes is formed by connecting, No. two density pond (3) volumes are 2 to 3 times of density pond (2) volume, a density pond (2) all sets out pipe material (4) with No. two density pond (3) bottoms, and be equipped with a square breach (5) above side, to realize the flowing of solidliquid mixture; Arrange breach between a density pond (2) and No. two density ponds (3) to enter No. two density ponds (3) by the post-depositional solidliquid mixture of one-level and carry out secondary deposition; Liquid after secondary deposition is discharged by No. two density ponds (3) opposite side setting party v notch v (5);
Described anaerobically fermenting mechanism is methane-generating pit, be arranged on raw materials pretreatment mechanism lower end, it adopts domes, be two skene arch compositions up and down, comprise more than 2 and pond of itemizing, each single pond comprises fermentation vat (6), feed-pipe (7), natural pond liquid storage pool (8), liquid discharge pipe (9) and airway (10), airway (10) is communicated with gas storage holder (11) with fermentation vat (6), described gas storage holder (11) is provided with two, each single pond gas storage holder (11) is collected to large gas-holder, natural pond liquid storage pool (8) in each single pond is pooled to natural pond liquid hold tank, be provided with liquid discharge pipe (9).
2. a kind of plant according to claim 1 biogas fermentation device, is characterized in that, is provided with stirrer at described Dan Chi top, improves attenuation degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420587251.XU CN204125315U (en) | 2014-10-13 | 2014-10-13 | A kind of plant biogas fermentation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420587251.XU CN204125315U (en) | 2014-10-13 | 2014-10-13 | A kind of plant biogas fermentation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204125315U true CN204125315U (en) | 2015-01-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420587251.XU Expired - Fee Related CN204125315U (en) | 2014-10-13 | 2014-10-13 | A kind of plant biogas fermentation device |
Country Status (1)
| Country | Link |
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| CN (1) | CN204125315U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106995237A (en) * | 2017-06-01 | 2017-08-01 | 段国昌 | A kind of unpowered automatic stirring and the methane production device for being recycled feed liquid |
| CN108585399A (en) * | 2018-04-12 | 2018-09-28 | 贵州工程应用技术学院 | Manure fermentation system |
| CN112452003A (en) * | 2020-12-04 | 2021-03-09 | 武汉派宁环保技术有限公司 | Environment-friendly pig wastewater treatment is with scraper blade preliminary sedimentation pond |
-
2014
- 2014-10-13 CN CN201420587251.XU patent/CN204125315U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106995237A (en) * | 2017-06-01 | 2017-08-01 | 段国昌 | A kind of unpowered automatic stirring and the methane production device for being recycled feed liquid |
| CN108585399A (en) * | 2018-04-12 | 2018-09-28 | 贵州工程应用技术学院 | Manure fermentation system |
| CN112452003A (en) * | 2020-12-04 | 2021-03-09 | 武汉派宁环保技术有限公司 | Environment-friendly pig wastewater treatment is with scraper blade preliminary sedimentation pond |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150128 Termination date: 20191013 |
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| CF01 | Termination of patent right due to non-payment of annual fee |