CN208097528U - A kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge - Google Patents
A kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge Download PDFInfo
- Publication number
- CN208097528U CN208097528U CN201820227559.1U CN201820227559U CN208097528U CN 208097528 U CN208097528 U CN 208097528U CN 201820227559 U CN201820227559 U CN 201820227559U CN 208097528 U CN208097528 U CN 208097528U
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- China
- Prior art keywords
- biogas
- shell
- shaft
- biogas residue
- discharge
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- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 46
- 239000012530 fluid Substances 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 10
- 238000007789 sealing Methods 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 claims description 3
- 239000002002 slurry Substances 0.000 abstract description 10
- 238000000926 separation method Methods 0.000 description 13
- 239000000203 mixture Substances 0.000 description 11
- 230000000694 effects Effects 0.000 description 8
- 238000000855 fermentation Methods 0.000 description 7
- 230000006872 improvement Effects 0.000 description 7
- 239000003337 fertilizer Substances 0.000 description 6
- 244000144977 poultry Species 0.000 description 6
- 210000003608 fece Anatomy 0.000 description 5
- 244000144972 livestock Species 0.000 description 5
- 239000003895 organic fertilizer Substances 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000010871 livestock manure Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000272525 Anas platyrhynchos Species 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- 241000282898 Sus scrofa Species 0.000 description 1
- 229930003779 Vitamin B12 Natural products 0.000 description 1
- VEUACKUBDLVUAC-UHFFFAOYSA-N [Na].[Ca] Chemical compound [Na].[Ca] VEUACKUBDLVUAC-UHFFFAOYSA-N 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- FDJOLVPMNUYSCM-WZHZPDAFSA-L cobalt(3+);[(2r,3s,4r,5s)-5-(5,6-dimethylbenzimidazol-1-yl)-4-hydroxy-2-(hydroxymethyl)oxolan-3-yl] [(2r)-1-[3-[(1r,2r,3r,4z,7s,9z,12s,13s,14z,17s,18s,19r)-2,13,18-tris(2-amino-2-oxoethyl)-7,12,17-tris(3-amino-3-oxopropyl)-3,5,8,8,13,15,18,19-octamethyl-2 Chemical compound [Co+3].N#[C-].N([C@@H]([C@]1(C)[N-]\C([C@H]([C@@]1(CC(N)=O)C)CCC(N)=O)=C(\C)/C1=N/C([C@H]([C@@]1(CC(N)=O)C)CCC(N)=O)=C\C1=N\C([C@H](C1(C)C)CCC(N)=O)=C/1C)[C@@H]2CC(N)=O)=C\1[C@]2(C)CCC(=O)NC[C@@H](C)OP([O-])(=O)O[C@H]1[C@@H](O)[C@@H](N2C3=CC(C)=C(C)C=C3N=C2)O[C@@H]1CO FDJOLVPMNUYSCM-WZHZPDAFSA-L 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000003630 growth substance Substances 0.000 description 1
- SEOVTRFCIGRIMH-UHFFFAOYSA-N indole-3-acetic acid Chemical compound C1=CC=C2C(CC(=O)O)=CNC2=C1 SEOVTRFCIGRIMH-UHFFFAOYSA-N 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000002917 insecticide Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000009527 percussion Methods 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000011715 vitamin B12 Substances 0.000 description 1
- 235000019163 vitamin B12 Nutrition 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
The utility model discloses it is a kind of can quick fluid-discharge biogas residue and biogas liquid seperator, including rack and be obliquely installed cylinder on the rack；Cylinder includes the shaft of shell and enclosure interior, and the outer diameter of shaft becomes larger from one end to the other end, and wherein upper end diameter is maximum；The outside of shaft is equipped with continuous helical blade；The top of shell one end is equipped with feed hopper, and lower part is equipped with the first leakage fluid dram；The shell other end is equipped with deslagging funnel；The lower section of housing central section is equipped with strainer, uniformly distributed several filter holes on strainer；The position that strainer is corresponded on shell is equipped with air guide, and flow-guiding channel is formed between air guide and shell, and the lower end of air guide is equipped with the second leakage fluid dram；Multiple notch are equipped at intervals on the outer edge of helical blade；The upper end interval of shaft is installed by multiple stirring rods.A kind of the advantages that biogas residue and biogas liquid seperator of energy quick fluid-discharge of the utility model, there are strainers to be not easy to plug for biogas residue and biogas liquid seperator, and biogas slurry discharge is smooth, and biogas residue and biogas liquid separative efficiency is high.
Description
Technical field
The utility model belongs to bioenergy equipment technology field more particularly to a kind of biogas residue and biogas liquid point of energy quick fluid-discharge
It disembarks.
Background technique
In recent years, aquaculture industry of China is grown rapidly, and is cultivated from small household to intensive large and medium-sized scale
Change farm's development, according to incompletely statistics, the large and medium-sized livestock and poultry farm in China has reached more than 26,000 ten thousand, annual excrement more than 40
Hundred million tons, agricultural stalk cannot recycle well.
Since China reforms and opens up to the outside world, country has put into effect system example about development new energy preferential policy, the pipe of environmental protection
Manage bar example, the poultry pollution problem of farm have become a big public hazards of society, and farm is to gather around to environmentally friendly procuratorial work, construction hair
Ferment device handles waste.Complete to ferment by natural temperature, marsh gas power generation project is risen in the whole nation, entirely middle cold fermentation technology, bacterium
Kind buys aerobic strain from society, and fermentation, which is not thorough, causes secondary pollution, and biogas residue and biogas liquid cannot utilize well.There are also biologies
Organic fertilizer field just produces organic fertilizer using family livestock and poultry, and pig manure chicken manure duck excrement is transported to place plus chemical deodorizing agent, dries in having made
Machine is fertile, and more than 360 a harmful bacterias, which cannot be discharged and be killed without hot fermentation, in excrement directly produces organic fertilizer, causes
Soil is shouted pollution.The small biogas project Chinese Ministry of Environmental Protection of secondary pollution are caused to shut down and rectified and improved much from 2016-2017, China's soil
The shout source of pollution, source is livestock and poultry feces, causes great damage to people's lives, and feces of livestock and poultry must be at high temperature anaerobic
Reason.
High-temperature anaerobic fermentation is carried out by raw material of cheap feces of livestock and poultry stalk, the feed degradation period can be shortened, thoroughly
Kill or discharge the harmful bacteria in waste.Big through high-temperature anaerobic fermentation gas production, every side's raw material produces 55 side of biogas or more.Biogas residue
Biogas slurry can make good biological organic fertilizer, and Liquid Fertilizer, guarantee is innoxious, and the waste heat of marsh gas power generation can be supplied with fermentation heat supply plant area
Dim, gas is used in organic fertilizer drying.Biogas slurry nutrient, such as N P and K sodium calcium through high-temperature anaerobic fermentation.Biogas residue and biogas liquid passes through certainly
The separation of dynamicization solid-liquid separating machine, biogas residue dry in, crush after, into whisking device ingredient, into fertilizer granulation machine production line, be granulated
Drying, it is cool but to pack organic solid fertilizer, biological multielement element fertilizer, flowers solid fertilizer etc. can also be produced.In biogas slurry through being separated by solid-liquid separation
Containing various bioactivators, such as amino acid, micro member thing, plant growth substance, vitamin B12, heteroauxin etc..It can
Blade face essence fertilizer is produced, soilless cultivation holds nutrient solution, can also do insecticide.
There are strainers easily to block for biogas residue and biogas liquid seperator in the prior art, and biogas slurry discharge is not thorough enough, detached job effect
The defects of rate is low, and biogas residue is more containing liquid after separation.
Summary of the invention
For disadvantages described above, technical problem to be solved in the utility model is:A kind of biogas residue of energy quick fluid-discharge is provided
Biogas slurry seperator, there are strainers to be not easy to plug for biogas residue and biogas liquid seperator, and biogas slurry discharge is smooth, and biogas residue and biogas liquid separative efficiency height etc. is excellent
Point.
In order to solve the above technical problems, the technical solution of the utility model is：
A kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge, including rack and the separation being inclined in the rack
Cylinder；The cylinder includes columned shell and the shaft for being rotatably arranged on the enclosure interior, the outer diameter of the shaft by
One end becomes larger to the other end, and wherein upper end diameter is maximum；The outside of shaft is equipped with continuous helical blade；The shell one
The top at end is equipped with feed hopper, and lower part is equipped with the first leakage fluid dram；The lower part of the shell other end is equipped with deslagging funnel；In the shell
The lower section in portion is equipped with strainer, uniformly distributed several filter holes on strainer；The position that strainer is corresponded on the shell is equipped with air guide, institute
The flow-guiding channel that formation is connected with cylinder between air guide and the shell is stated, the lower end of the air guide is equipped with second
Leakage fluid dram；Multiple notch are equipped at intervals on the outer edge of the helical blade；The upper end interval of the shaft is installed by multiple stirrings
Bar, stirring rod are convenient for the discharge of biogas residue with shaft rotation.
As an improvement the screw pitch of the helical blade is gradually become smaller from the lower end of shaft to upper end.
As an improvement the upper end of the shaft is machined with the chamfering of arcuation.
As an improvement being equipped with elastic sealing gasket between the diversion pipe and the shell.
As an improvement the notch is serrated.
As an improvement the shaft and first motor are sequentially connected, first motor is fixedly mounted in the rack.
As an improvement the angle of the cylinder and horizontal plane is 8 °~10 °.
Using above-mentioned technical proposal, the utility model has the beneficial effects that：
1, the mixture of biogas residue and biogas liquid puts into cylinder by the feed hopper of seperator lower end, and helical blade rotates simultaneously with shaft
Drive the deslagging funnel conveying of the mixture of biogas residue and biogas liquid obliquely upward, mixture of the transmission process helical blade to biogas residue and biogas liquid
It is squeezed, isolated liquid is discharged by the first leakage fluid dram or by filter opening and flow-guiding channel by the second leakage fluid dram.
2, cylinder tilts upward setting, which has the function of drip except liquid；The outer diameter of shaft becomes larger,
Has the function of extruding mixture, so that solid-liquid separation effect is more preferable.
3, multiple notch are equipped at intervals on the outer edge of helical blade, notch is to the filter near filter opening when helical blade rotates
Net has cleaning effect, will be attached to the substance near filter opening and removes, can effectively prevent the blocking of strainer, the filtrate after separation can
To be smoothly discharged.
4, multiple stirring rods are installed at the upper end interval of shaft, and stirring rod is convenient for the discharge of biogas residue with shaft rotation.
5, the screw pitch of helical blade is gradually become smaller from the lower end of shaft to upper end, reinforces helical blade to output end mixture
Extruding so that be separated by solid-liquid separation effect it is more preferable.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of the embodiment of the biogas residue and biogas liquid seperator of energy quick fluid-discharge of the utility model.
Fig. 2 is A-A cross-sectional view in Fig. 1.
Fig. 3 is enlarged drawing at B in Fig. 1.
Wherein：1- rack, 2- cylinder, 21- shell, 211- feed hopper, the first leakage fluid dram of 212-, 213- deslagging funnel,
214- strainer, 215- filter hole, 22- shaft, 221- chamfering, 23- helical blade, 231- notch, 24- stirring rod, 3- air guide,
31- flow-guiding channel, the second leakage fluid dram of 32-, 4- elastic sealing gasket, 5- overflow pipe, 6- discharge mechanism, 61- rotary shaft, 62- are scraped
Plate, 7- first motor.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only to explain this
Utility model is not used to limit the utility model.
Embodiment
It is jointly shown by Fig. 1, Fig. 2 and Fig. 3, a kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge, including rack 1 and setting
Cylinder 2 in rack 1, cylinder 2 tilt upward setting, and cylinder 2 and the angle of horizontal plane are 8 °~10 °.Cylinder 2
Setting is tilted upward, which has the function of drip except liquid, convenient for the precipitation of liquid substance.Cylinder 2 includes cylinder
The shell 21 of shape and the shaft 22 being rotatably arranged on inside shell 21.Shaft 22 and first motor 7 are sequentially connected, first motor 7
It is fixedly mounted in rack 1.
Jointly shown by Fig. 1, Fig. 2 and Fig. 3, the top of 21 one end of shell is equipped with feed hopper 211, and lower part is equipped with the first drain
Mouth 212；The lower part of 21 other end of shell is equipped with deslagging funnel 213.The lower section at the middle part of shell 21 is equipped with strainer 214, on strainer 214
Uniformly distributed several filter holes 215.The position that strainer 214 is corresponded on shell 21 is equipped with air guide 3, between air guide 3 and shell 21
The flow-guiding channel 31 being connected with cylinder 2 is formed, the lower end of air guide 3 is equipped with the second leakage fluid dram 32.Diversion pipe and shell
Elastic sealing gasket 4 is equipped between 21.The middle part of feed hopper 211 connects overflow pipe 5.The conveying of helical blade 23 and extruding biogas residue and biogas liquid again
Mixture when, due to the mutual extrusion and percussion between helical blade 23 and biogas residue and biogas liquid, cause biogas residue and biogas liquid from charging
The overflow pipe 5 of bucket 211 flows out, and will not directly overflow from feed inlet, cause the pollution of operating environment.It is equipped in deslagging funnel 213
Rotate the discharge mechanism 6 of setting.Discharge mechanism 6 includes rotary shaft 61 and the scraper plate 62 that multiple intervals are mounted in rotary shaft 61.
Rotary shaft 61 is connect with the second motor drive.Rotary shaft 61 drives the rotation of scraper plate 62 can will be to the biogas residue after separation from cylinder
2 send to deslagging funnel 213, and convenient for being smoothly discharged of biogas residue, slag-drip opening is not easy to plug.
Jointly shown by Fig. 1, Fig. 2 and Fig. 3, the outer diameter of shaft 22 becomes larger from one end to the other end, and upper end diameter is most
Greatly, 22 outside diameter of shaft is twice of end diameter.The outer diameter of shaft 22 becomes larger, and has the function of extruding mixture,
So that solid-liquid separation effect is more preferable.The upper end of shaft 22 is machined with the chamfering 221 of arcuation.The outside of shaft 22 is equipped with continuous spiral shell
The screw pitch of vane piece 23, helical blade 23 is gradually become smaller from the lower end of shaft 22 to upper end, can reinforce helical blade 23 to defeated
The extruding of outlet mixture, so that the effect being separated by solid-liquid separation is more preferable.Multiple sawtooth are equipped at intervals on the outer edge of helical blade 23
The notch 231 of shape.Multiple notch 231 are equipped at intervals on the outer edge of helical blade 23, notch 231 is right when helical blade 23 rotates
Strainer 214 near filter opening has cleaning effect, will be attached to the substance near filter opening and removes, can effectively prevent strainer 214
Blocking, the filtrate after separation can be smoothly discharged.Multiple stirring rods 24 are installed at the upper end interval of shaft 22, and stirring rod 24 is with shaft
The discharge of biogas residue is convenient in 22 rotations.
In use, the mixture of biogas residue and biogas liquid puts into cylinder 2, helical blade 23 by the feed hopper 211 of seperator lower end
It is rotated with shaft 22 and the deslagging funnel 213 of the mixture of biogas residue and biogas liquid obliquely upward is driven to convey, helical-blade in transmission process
Piece 23 squeezes the mixture of biogas residue and biogas liquid.The biogas slurry isolated is led to by the first leakage fluid dram 212 or by filter opening and water conservancy diversion
Road 31 is discharged by the second leakage fluid dram 32, and the biogas residue isolated is discharged by deslagging funnel 213.
In conclusion a kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge of the utility model, it can be by biogas residue and biogas slurry
Separated, and separative efficiency is high, strainer is not easy to plug, and biogas slurry discharge is smooth, after separation biogas residue can be smoothly discharged, slag-drip opening not
Easily blocking, and biogas residue and biogas liquid will not occur in separation process and overflowed from feed hopper.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model
Protection scope within.
Claims (7)
1. a kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge, it is characterised in that：Including rack (1) and it is inclined at the machine
Cylinder (2) on frame (1)；The cylinder (2) includes columned shell (21) and is rotatably arranged on the shell (21)
Internal shaft (22), the outer diameter of the shaft (22) become larger from one end to the other end, and wherein upper end diameter is maximum；Shaft
(22) outside is equipped with continuous helical blade (23)；
The top of described shell (21) one end is equipped with feed hopper (211), and lower part is equipped with the first leakage fluid dram (212)；Shell (21) is another
The lower part of one end is equipped with deslagging funnel (213)；Lower section in the middle part of the shell (21) is equipped with strainer 214, is evenly distributed on strainer (214)
Several filter holes (215)；
The position that strainer (214) is corresponded on the shell (21) is equipped with air guide (3), the air guide (3) with it is described
The flow-guiding channel (31) being connected with cylinder (2) is formed between shell (21), the lower end of the air guide (3) is equipped with second row
Liquid mouth (32)；Multiple notch (231) are equipped at intervals on the outer edge of the helical blade (23)；Between the upper end of the shaft (22)
Every installing multiple stirring rods (24), stirring rod (24) is convenient for the discharge of biogas residue with shaft (22) rotation.
2. the biogas residue and biogas liquid seperator of energy quick fluid-discharge according to claim 1, it is characterised in that：The helical blade
(23) screw pitch is gradually become smaller from the lower end of shaft (22) to upper end.
3. the biogas residue and biogas liquid seperator of energy quick fluid-discharge according to claim 2, it is characterised in that：The shaft (22)
Upper end is machined with the chamfering (221) of arcuation.
4. the biogas residue and biogas liquid seperator of energy quick fluid-discharge according to claim 3, it is characterised in that：The air guide
(3) elastic sealing gasket (4) are equipped between the shell (21).
5. the biogas residue and biogas liquid seperator of energy quick fluid-discharge according to claim 4, it is characterised in that：The notch (231)
It is serrated.
6. the biogas residue and biogas liquid seperator of energy quick fluid-discharge according to claim 5, it is characterised in that：The shaft (22) with
First motor (7) transmission connection, first motor (7) are fixedly mounted on the rack (1).
7. the biogas residue and biogas liquid seperator of energy quick fluid-discharge according to claim 6, it is characterised in that：The cylinder (2)
Angle with horizontal plane is 8 °~10 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820227559.1U CN208097528U (en) | 2018-02-07 | 2018-02-07 | A kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820227559.1U CN208097528U (en) | 2018-02-07 | 2018-02-07 | A kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208097528U true CN208097528U (en) | 2018-11-16 |
Family
ID=64123861
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820227559.1U Expired - Fee Related CN208097528U (en) | 2018-02-07 | 2018-02-07 | A kind of biogas residue and biogas liquid seperator of energy quick fluid-discharge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208097528U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117483219A (en) * | 2023-12-26 | 2024-02-02 | 佛山市扬子颜料有限公司 | Printing ink particle size separation device |
| CN117483219B (en) * | 2023-12-26 | 2024-04-26 | 佛山市扬子颜料有限公司 | Printing ink particle size separation device |
-
2018
- 2018-02-07 CN CN201820227559.1U patent/CN208097528U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117483219A (en) * | 2023-12-26 | 2024-02-02 | 佛山市扬子颜料有限公司 | Printing ink particle size separation device |
| CN117483219B (en) * | 2023-12-26 | 2024-04-26 | 佛山市扬子颜料有限公司 | Printing ink particle size separation device |
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|---|---|---|---|
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| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181116 |
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| CF01 | Termination of patent right due to non-payment of annual fee |