CN204643954U - Poultry large-scale cultivation highly effective anaerobic reaction tank - Google Patents
Poultry large-scale cultivation highly effective anaerobic reaction tank Download PDFInfo
- Publication number
- CN204643954U CN204643954U CN201520239782.4U CN201520239782U CN204643954U CN 204643954 U CN204643954 U CN 204643954U CN 201520239782 U CN201520239782 U CN 201520239782U CN 204643954 U CN204643954 U CN 204643954U
- Authority
- CN
- China
- Prior art keywords
- reaction tank
- anaerobic reaction
- central duct
- water distribution
- triphase separator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a kind of poultry large-scale cultivation highly effective anaerobic reaction tank, central duct is provided with in anaerobic reaction tank central position, water distribution pipe is fixed with by fixed support bottom central duct, water distribution pipe is made up of 6 water distribution laterals, a reflection cone is provided with below every root water distribution lateral end, central duct and anaerobic reaction tank top institute contact position are provided with adapter bonnet, in central duct upper end, sidepiece is provided with inlet channel, inlet channel is connected by the 6 water distribution laterals in central duct and bottom, anaerobic reaction tank top is provided with gas exhaust duct, sidepiece is provided with drainage pipeline, gas exhaust duct tip height is lower than inlet channel height, drainage pipeline tip height is lower than gas exhaust duct tip height.The utility model utilizes the height fall of the hydraulic pressure after adapter bonnet reducing, effluent sewage self gravitation and central duct, enables effluent sewage fully carry out anaerobically fermenting reaction, and guarantee gas, dirt are effectively separated, and improve biogas production rate.
Description
Technical field:
The utility model relates to a kind of breeding enterprise anaerobic reaction device, particularly relates to a kind of poultry large-scale cultivation highly effective anaerobic reaction tank.
Background technology:
All there is treatment for cow manure biogas engineering in Large-scale professional enterprise of raising pigs, general employing anaerobic digestion techniques processes the effluent sewage of a large amount of livestock on hand live pig, effluent sewage after precipitation, waste water is transported in anaerobic reactor and processes, the natural pond liquid that the biogas produced after process can be used as generating electricity, produce for field irrigation, thus achieves the resource utilization of pig farm effluent sewage, innoxious and ecology recycling after aerobic treatment.But in prior art, upper end, anaerobic reactor side is provided with inlet channel, opposite side is provided with drainage pipeline, sewage is discharged soon in anaerobic reactor, gas, dirt effectively can not be separated, to breeding enterprise normally produce process and health qualified discharge bring disadvantageous effect, work the mischief to surrounding environment.
Utility model content:
Technical problem to be solved in the utility model is: provide a kind of poultry large-scale cultivation highly effective anaerobic reaction tank that can ensure gas, dirty fully effective separation, has the useless dirty advantage such as timely of reasonable in design, quick and high efficient reaction, process.
The technical scheme that the utility model is taked for technical solution problem is:
A kind of poultry large-scale cultivation highly effective anaerobic reaction tank, comprise anaerobic reaction tank, described anaerobic reaction tank central position is provided with central duct, the height of described central duct is 5/3 of described anaerobic reaction tank height, described central duct runs through described anaerobic reaction tank, water distribution pipe is fixedly installed by fixed support bottom described central duct, described water distribution pipe is made up of 6 water distribution laterals, 6 water distribution laterals with bottom described central duct for the center of circle is uniformly distributed, angle often between adjacent two water distribution laterals is 60 degree, a reflection cone is provided with below the end of every root water distribution lateral, the cross section of described reflection cone is triangular shaped in obtuse angle, between sidepiece and bottom, angle is 30 degree, described central duct and described anaerobic reaction tank top institute contact position are 800mm*600mm adapter bonnet, and described central duct upper end sidepiece is provided with inlet channel, and described inlet channel is connected by the 6 water distribution laterals in described central duct and bottom, it is described that anaerobic reaction tank top is provided with gas exhaust duct, sidepiece is provided with drainage pipeline, inside described anaerobic reaction tank, upper position installs and is equipped with triphase separator, the height on described gas exhaust duct top is lower than the height of described inlet channel, and the height on described drainage pipeline top is lower than the height on described gas exhaust duct top.
Described triphase separator comprises triphase separator overhead gage and triphase separator lower shoe, described triphase separator overhead gage and triphase separator lower shoe parallel to each other, described triphase separator overhead gage upper end is fixed on central duct outer wall, middle part is fixed on described central duct outer wall by channel-section steel fixed support, and the angle between described triphase separator overhead gage upper end and central duct outer wall is 60 degree; Described triphase separator lower shoe lower end is fixed in anaerobic reaction-pot inner tank wall, middle part is fixed in described anaerobic reaction-pot inner tank wall by base plate lower bracket, angle between described triphase separator lower shoe lower end and described anaerobic reaction-pot inner tank wall is 120 degree, be positioned at the upper end of described triphase separator overhead gage bottom described gas exhaust duct, facilitate the effusion of gas.
Described anaerobic reaction tank top is oval structure, described anaerobic reaction-pot tank base is provided with bottom stationary bearing, described bottom stationary bearing is provided with the spoil disposal mouth of pipe; Described inlet channel is provided with water inlet control valve, described drainage pipeline is provided with outlet water control valve.
Described fixed support is made up of vertical supporting rod and support rail, described support rail is 12,6 length 6 are short, 6 hyphen bars are welded to each other and form little regular hexagon together, 6 long transverse levers are welded to each other and form large regular hexagon together, described little regular hexagon is sleeved in described large regular hexagon, and described 6 water distribution laterals are fixedly welded on each summit of described little regular hexagon and described large regular hexagon formation respectively; Described little regular hexagon and described large regular hexagon each summit place are vertically installed with a vertical supporting rod respectively, described vertical supporting rod is 12, length is consistent, and the top of 12 vertical supporting rods is welded on described little regular hexagon respectively and described large regular hexagon each summit place, bottom are welded on the bottom stationary bearing of described anaerobic reaction-pot tank base.
Positive beneficial effect of the present utility model is as follows:
1, the utility model by being fixedly installed 6 water distribution laterals bottom central duct, a reflection cone is provided with below the end of every root water distribution lateral, inlet channel is connected with respective reflection cone with 6 water distribution laterals through after central duct from top to bottom, utilize the gravity of effluent sewage self and the drop of central duct height, effluent sewage enters in anaerobic reaction-pot by 6 trilateral reflection cone reflections, stirring up and down and circulating along with liquid, effluent sewage can carry out sufficient anaerobically fermenting reaction, ensure gas, dirt is effectively separated, improve biogas production rate.
2,6 trilateral reflection cones of the present utility model are positioned in concentric circumferences, and each water distribution reflection cone is uniformly distributed, can increase on the one hand each water outlet area coverage, improve the homogeneity of anaerobic reactor water distribution; On the other hand, the water outlet hydraulic pressure of each water distribution reflection cone is completely the same, strengthen into water and base sludge layer abundant mixing with contact, improve gas, dirty purification separation effect.
3, the top of the utility model anaerobic reaction tank is oval structure, there is not reaction Dead Core Problems in retort, facilitates liquids and gases to overturn mixing back and forth in anaerobic reaction tank, and make reaction more thorough, separating effect is more thorough.
4, the utility model is by being provided with 800mm*600mm adapter bonnet at center inlet channel and anaerobic reaction tank institute contact position, increase effluent sewage enters the pressure in tank body, add the gravity of effluent sewage self and the drop of central duct height, gas, dirty purification separation effect are more abundant.
5, triphase separator of the present utility model comprises triphase separator overhead gage and triphase separator lower shoe, triphase separator overhead gage and triphase separator lower shoe parallel to each other, be fixed in central duct outer wall and anaerobic reaction-pot inner tank wall respectively by support, the reflection being easier to solid, liquid, gas be separated.
6, the utility model has the useless dirty advantage such as timely of reasonable in design, quick and high efficient reaction, process, normally produces the dirty and health qualified discharge of process excrement establish solid technical foundation for breeding enterprise.
Accompanying drawing illustrates:
Fig. 1 is one of structural representation of the present utility model;
Fig. 2 is structural representation two of the present utility model;
Fig. 3 is the fragmentary bottom structural representation of water distribution pipe in Fig. 1;
Fig. 4 is the structure for amplifying schematic diagram of reflection cone in Fig. 1.
Embodiment:
Below in conjunction with accompanying drawing, the utility model is further explained and illustrate:
See Fig. 1, a kind of poultry large-scale cultivation highly effective anaerobic reaction tank, comprise anaerobic reaction tank 13, anaerobic reaction tank 13 central position is provided with central duct 3, the height of central duct 3 is 5/3 of anaerobic reaction tank 13 height, central duct 3 runs through anaerobic reaction tank 13, water distribution pipe 15 is fixedly installed by fixed support 14 bottom central duct 3, water distribution pipe 15 is made up of 6 water distribution laterals, 6 water distribution laterals with bottom central duct 3 for the center of circle is uniformly distributed, angle often between adjacent two water distribution laterals is 60 degree, a reflection cone 16 is provided with below the end of every root water distribution lateral, the cross section of reflection cone 16 is triangular shaped in obtuse angle, between sidepiece and bottom, angle is 30 degree, central duct 3 and anaerobic reaction tank 13 top institute contact position are provided with 800mm*600mm adapter bonnet 5, and central duct 3 upper end sidepiece is provided with inlet channel 1, and inlet channel 1 is connected by the 6 water distribution laterals in central duct 3 and bottom, anaerobic reaction tank 13 top is provided with gas exhaust duct 4, sidepiece is provided with drainage pipeline 7, inside anaerobic reaction tank 13, upper position installs and is equipped with triphase separator, the height on gas exhaust duct 4 top is lower than the height of inlet channel 1, and the height on drainage pipeline 7 top is lower than the height on gas exhaust duct 4 top.
Triphase separator comprises triphase separator overhead gage 9 and triphase separator lower shoe 11, triphase separator overhead gage 9 and triphase separator lower shoe 11 parallel to each other, triphase separator overhead gage 9 upper end is fixed on central duct 3 outer wall, middle part is fixed on central duct 3 outer wall by channel-section steel fixed support 10, and the angle between triphase separator overhead gage 9 upper end and central duct 3 outer wall is 60 degree; Triphase separator lower shoe 11 lower end is fixed on anaerobic reaction tank 13 inwall, middle part is fixed on anaerobic reaction tank 13 inwall by base plate lower bracket 12, angle between triphase separator lower shoe 11 lower end and anaerobic reaction tank 13 wall is 120 degree, be positioned at the upper end of triphase separator overhead gage 9 bottom gas exhaust duct 4, facilitate the effusion of gas.
Anaerobic reaction tank 13 top is oval structure 6, is provided with bottom stationary bearing 17, bottom stationary bearing 17 is provided with the spoil disposal mouth of pipe 18 bottom anaerobic reaction tank 1; Inlet channel 1 is provided with water inlet control valve 2, drainage pipeline 7 is provided with outlet water control valve 8.
Described fixed support 14 is made up of vertical supporting rod 19 and support rail 20, support rail 20 is 12,6 length 6 are short, 6 hyphen bars are welded to each other and form little regular hexagon together, 6 long transverse levers are welded to each other and form large regular hexagon together, described little regular hexagon is sleeved in described large regular hexagon, and described 6 water distribution laterals are fixedly welded on each summit of described little regular hexagon and described large regular hexagon formation respectively; A vertical supporting rod 19 is vertically installed with respectively at little regular hexagon and described large regular hexagon each summit place, vertical supporting rod 19 is also 12, length is consistent, and the top of 12 vertical supporting rods 19 is welded on little regular hexagon respectively and large regular hexagon each summit place, bottom are welded on the bottom stationary bearing 17 bottom anaerobic reaction tank 13.
The utility model utilizes the caliber of the gravity of effluent sewage self, the drop of central duct height and center adapter bonnet to change, effluent sewage flows in anaerobic reaction-pot by 6 trilateral reflection cones, stirring up and down and circulating along with liquid, effluent sewage can carry out sufficient anaerobically fermenting reaction, guarantee gas, dirt are effectively separated, and improve biogas production rate.
The above; it is only preferred embodiment of the present utility model; not any pro forma restriction is done to the utility model; every above embodiment is done according to technical spirit of the present utility model any simple modification, equivalent variations and modification, within the protection domain all still belonging to technical solutions of the utility model.
Claims (4)
1. a poultry large-scale cultivation highly effective anaerobic reaction tank, comprise anaerobic reaction tank (13), it is characterized in that: described anaerobic reaction tank (13) central position is provided with central duct (3), the height of described central duct (3) is 5/3 of described anaerobic reaction tank (13) height, described central duct (3) runs through described anaerobic reaction tank (13), water distribution pipe (15) is fixedly installed by fixed support (14) in described central duct (3) bottom, described water distribution pipe (15) is made up of 6 water distribution laterals, 6 water distribution laterals with described central duct (3) bottom for the center of circle is uniformly distributed, angle often between adjacent two water distribution laterals is 60 degree, a reflection cone (16) is provided with below the end of every root water distribution lateral, the cross section of described reflection cone (16) is triangular shaped in obtuse angle, between sidepiece and bottom, angle is 30 degree, described central duct (3) and described anaerobic reaction tank (13) top institute contact position are 800mm*600mm adapter bonnet (5), described central duct (3) upper end sidepiece is provided with inlet channel (1), and described inlet channel (1) is connected by the 6 water distribution laterals in described central duct (3) and bottom, described anaerobic reaction tank (13) top is provided with gas exhaust duct (4), sidepiece is provided with drainage pipeline (7), described anaerobic reaction tank (13) the inside upper position installs and is equipped with triphase separator, the height on described gas exhaust duct (4) top is lower than the height of described inlet channel (1), and the height on described drainage pipeline (7) top is lower than the height on described gas exhaust duct (4) top.
2. poultry large-scale cultivation highly effective anaerobic reaction tank according to claim 1, it is characterized in that: described triphase separator comprises triphase separator overhead gage (9) and triphase separator lower shoe (11), described triphase separator overhead gage (9) and triphase separator lower shoe (11) parallel to each other, described triphase separator overhead gage (9) upper end is fixed on central duct (3) outer wall, middle part is fixed on described central duct (3) outer wall by channel-section steel fixed support (10), angle between described triphase separator overhead gage (9) upper end and central duct (3) outer wall is 60 degree, described triphase separator lower shoe (11) lower end is fixed on anaerobic reaction tank (13) inwall, middle part is fixed on described anaerobic reaction tank (13) inwall by base plate lower bracket (12), angle between described triphase separator lower shoe (11) lower end and described anaerobic reaction tank (13) inwall is 120 degree, described gas exhaust duct (4) bottom is positioned at the upper end of described triphase separator overhead gage (9), facilitates the effusion of gas.
3. poultry large-scale cultivation highly effective anaerobic reaction tank according to claim 1, it is characterized in that: described anaerobic reaction tank (13) top is oval structure (6), described anaerobic reaction tank (1) bottom is provided with bottom stationary bearing (17), described bottom stationary bearing (17) is provided with the spoil disposal mouth of pipe (18); Described inlet channel (1) is provided with water inlet control valve (2), described drainage pipeline (7) is provided with outlet water control valve (8).
4. poultry large-scale cultivation highly effective anaerobic reaction tank according to claim 3, it is characterized in that: described fixed support (14) is made up of vertical supporting rod (19) and support rail (20), described support rail (20) is 12,6 length 6 are short, 6 hyphen bars are welded to each other and form little regular hexagon together, 6 long transverse levers are welded to each other and form large regular hexagon together, described little regular hexagon is sleeved in described large regular hexagon, and described 6 water distribution laterals are fixedly welded on each summit of described little regular hexagon and described large regular hexagon formation respectively; Described little regular hexagon and described large regular hexagon each summit place are vertically installed with a vertical supporting rod (19) respectively, described vertical supporting rod (19) is 12, length is consistent, and the top of 12 vertical supporting rods (19) is welded on described little regular hexagon respectively and described large regular hexagon each summit place, bottom are welded on the bottom stationary bearing (17) of described anaerobic reaction tank (13) bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520239782.4U CN204643954U (en) | 2015-04-21 | 2015-04-21 | Poultry large-scale cultivation highly effective anaerobic reaction tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520239782.4U CN204643954U (en) | 2015-04-21 | 2015-04-21 | Poultry large-scale cultivation highly effective anaerobic reaction tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204643954U true CN204643954U (en) | 2015-09-16 |
Family
ID=54096720
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520239782.4U Withdrawn - After Issue CN204643954U (en) | 2015-04-21 | 2015-04-21 | Poultry large-scale cultivation highly effective anaerobic reaction tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204643954U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104761053A (en) * | 2015-04-21 | 2015-07-08 | 牧原食品股份有限公司 | Efficient anaerobic reaction tank for large-scale raising of livestock |
-
2015
- 2015-04-21 CN CN201520239782.4U patent/CN204643954U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104761053A (en) * | 2015-04-21 | 2015-07-08 | 牧原食品股份有限公司 | Efficient anaerobic reaction tank for large-scale raising of livestock |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104098236B (en) | Large-scale penkeeping field sewage treatment process | |
| CN203904338U (en) | Double-path reflux anaerobic reaction system and reactor for producing biogas by using straw | |
| CN104817170A (en) | Large-scale piggery dung treatment ecological circulation system | |
| CN104649530A (en) | Method of treating feces in breeding industry | |
| CN101817586A (en) | Spiral-flow water-distribution hydrocyclone internal-circulation anaerobic reactor | |
| CN102690754A (en) | Combined anaerobic fermentation tank | |
| CN204643958U (en) | Modernization pig house wastewater reuse approach anaerobic reaction system | |
| CN204550559U (en) | A kind of changing food waste is from stirring anaerobic digestion biogas production equipment | |
| CN204079592U (en) | A kind of EGSB reactor water-distributing device | |
| CN201362614Y (en) | Internal circulation anaerobic reactor for cyclone water distribution cyclone separation | |
| CN204643954U (en) | Poultry large-scale cultivation highly effective anaerobic reaction tank | |
| CN203820526U (en) | Aerobic pool for sewage treatment and sewage treatment device | |
| CN201878622U (en) | Turtle culture circulation system | |
| CN206244783U (en) | A kind of van-type anaerobic ferment devices | |
| CN104761053B (en) | Poultry large-scale cultivation anaerobic reaction-pot | |
| CN204588928U (en) | A kind of poultry sewage discharge system based on EGSB | |
| CN103087902B (en) | Automatic crusting-breaking gas producing and storing wet type integrated anaerobic fermentation device | |
| CN204643953U (en) | Water distribution reflection cone bottom the anaerobic reaction device of pig farm | |
| CN202717772U (en) | Combined anaerobic fermentation tank | |
| CN208008791U (en) | A kind of biogas anaerobic reactor aeration plug-flow pipe | |
| CN201801519U (en) | Biogas storage tank | |
| CN201406367Y (en) | Duplex-ball-heated multistage fermentation biogas tank | |
| CN204737845U (en) | Dirty wholeization processing system of pig farm excrement | |
| CN103803702B (en) | Small mechanized anaerobic reactor | |
| CN204644064U (en) | The useless dirty cycle for the treatment of re-use device of cultivation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150916 Effective date of abandoning: 20161012 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |