CN204737845U - Dirty wholeization processing system of pig farm excrement - Google Patents
Dirty wholeization processing system of pig farm excrement Download PDFInfo
- Publication number
- CN204737845U CN204737845U CN201520239950.XU CN201520239950U CN204737845U CN 204737845 U CN204737845 U CN 204737845U CN 201520239950 U CN201520239950 U CN 201520239950U CN 204737845 U CN204737845 U CN 204737845U
- Authority
- CN
- China
- Prior art keywords
- inlet channel
- anaerobic reaction
- highly effective
- reaction tank
- excrement
- 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.)
- Active
Links
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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a dirty wholeization processing system of pig farm excrement, utilize the unit including the dirty collector unit of excrement, solid -liquid separation unit, anaerobic fermentation unit, biogas utilization unit and natural pond liquid, the high - rate anaerobic reaction jar of anaerobic fermentation unit for being provided with backflow pipeline, through being provided with central inlet channel in high - rate anaerobic reaction jar center, center inlet channel bottom is provided with 6 water distribution lateral conduits, tip below at every water distribution lateral conduit is provided with reflection cone, inlet channel from the top down is linked together with 6 water distribution lateral conduits and respective reflection cone after passing central inlet channel, utilize the gravity of excrement sewage self, the drop of central tube height and the reducing effect of central inlet tube, excrement sewage passes through the reflection cone reflection and gets into in the high - rate anaerobic reaction jar, along with the upper and lower of liquid turns and circulate, excrement sewage can carry out abundant anaerobic fermentation reaction, guarantee gas, liquid, admittedly it effectively separates to carry out the three -phase, improve the dirty integrated treatment effect of pig farm excrement.
Description
Technical field:
The utility model relates to a kind for the treatment of for cow manure system, particularly relate to the dirty integration treatment system of a kind of pig farm excrement, by adopting solid-liquid separation and efficient anaerobic fermentation technology, first excrement sewage is separated into argol and liquid dung, argol becomes fertilizer through process, liquid dung produces biogas and natural pond liquid through efficient anaerobic fermentation, and biogas can be used for generating, natural pond liquid and can be used for pouring farmland and trees.
Background technology:
Along with the development of livestock industry; Large-scale pig farm increases progressively fast with region of raising pigs; the subject matter brought is exactly the process problem of bulky stool sewage and waste water: because the leaching of fecaluria is very strong; if do not dealt carefully with; Water table will be entered by rainwash and diafiltration; or accumulate in soil, cause soil pollution.Fecaluria outdoor storeyard in pig farm is the main path causing surface water, groundwater pollution at the rainwash in rainy season.Therefore, how effective pig farm fecaluria for large-scale cultivation carries out effectively process is significant problem urgently to be resolved hurrily at present.If there is a kind of way effectively can process the excrement sewage of cultivation generation and carry out excrement dirt recycling, so just can saves great expense to aquaculture, improve the dirty comprehensive utilization ratio of excrement.
Utility model content:
Technical problem to be solved in the utility model is: provide a kind of pig farm excrement dirty integration treatment system, excrement sewage not only can be made to produce biogas and natural pond liquid through high-efficiency fermenting reaction, fertilizer can also be produced through solid-liquid separation, make excrement dirt reach organic recycling of the close-coupled processing and energy efficiently, improve useless dirty comprehensive utilization ratio.
The technical scheme that the utility model is taked for technical solution problem is:
The dirty integration treatment system of a kind of pig farm excrement, comprise excrement dirty collector unit, solid-liquid separation unit, anaerobically fermenting unit, biogas utilization unit and natural pond liquid range site, the dirty collector unit of described excrement comprises filtering basin, stercoroma pond and Buffer Pool, after the excrement sewage ejected from pig house is filtered by filtering basin, waste liquid is drained in Buffer Pool, the dirt of solid excrement is transported in stercoroma pond, described solid-liquid separation unit comprises solid-liquid separating machine and fertilizer treatment unit, and after the solid excrement soiled ends in described stercoroma pond crosses solid-liquid separating machine process, solid matter carries out processing through fertilizer treatment unit, liquid flow in described Buffer Pool, described anaerobically fermenting unit is highly effective anaerobic reaction tank, and the waste water in described Buffer Pool enters into highly effective anaerobic reaction tank and carries out anaerobically fermenting process after lift pump promotes, described biogas utilization unit comprises biogas cabinet, methane purifying device and biogas electricity generation apparatus, the biogas produced in described highly effective anaerobic reaction tank enters in described biogas cabinet through getter pipeline, exports the biogas come and be input in biogas electricity generation apparatus after methane purifying device purification from biogas cabinet, described natural pond liquid range site comprises natural pond liquid storage pool, forestry irrigation rig and farmland irrigating device, the natural pond liquid produced in described highly effective anaerobic reaction tank flows in the liquid storage pool of natural pond through natural pond liquid transport pipe, as required, the natural pond liquid of natural pond liquid storage pool flows into respectively in forestry irrigation rig and farmland irrigating device and utilizes, described highly effective anaerobic reaction tank central position is provided with center inlet channel, the height of described center inlet channel is 5/3 of described highly effective anaerobic reaction tank height, described center inlet channel runs through described highly effective anaerobic reaction tank, water distribution pipe is fixedly installed by fixed support bottom the inlet channel of described center, described water distribution pipe is made up of 6 water distribution laterals, 6 water distribution laterals with bottom the inlet channel of described center 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 trilateral in obtuse angle of described reflection cone, between sidepiece and bottom, angle is 30 degree, adapter bonnet centered by described center inlet channel and described highly effective anaerobic reaction tank top institute contact position, inlet channel upper end one, described center sidepiece is provided with inlet channel, the other side is provided with gas exhaust duct and reflux line, and described inlet channel is connected by the 6 water distribution laterals in described center inlet channel and bottom, described highly effective anaerobic reaction upper end sidepiece is provided with drainage pipeline, inside described highly effective anaerobic reaction tank, upper position installs and is equipped with triphase separator, described highly effective anaerobic reaction pot bottom is provided with firm banking, is provided with sludge discharging port and observes manhole above described firm banking, the water inlet height of height higher than the water inlet height of described inlet channel, described inlet channel of giving vent to anger of described gas exhaust duct is higher than the drain height of the water inlet height bottom the freeboard on described reflux line top, described reflux line higher than described drainage pipeline.
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 provided 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 firm banking of described highly effective anaerobic reaction pot bottom.
Described highly effective anaerobic reaction tank top is oval structure, 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 the outer wall of described center inlet channel, angle between described triphase separator overhead gage upper end and center inlet channel outer wall is 60 degree, the tapered distribution of described triphase separator overhead gage; Described triphase separator lower shoe lower end is fixed on the inwall of described highly effective anaerobic reaction tank, and the angle between described triphase separator lower shoe lower end and described highly effective anaerobic reaction top tank structure is 120 degree, and described triphase separator lower shoe is annular distribution; The water port of described drainage pipeline is positioned at the upper end of described triphase separator.
Described inlet channel is provided with water inlet control valve door, described gas exhaust duct is provided with gas exhaust inspecting valve, described drainage pipeline is provided with draining control valve door.
The utility model is by adopting solid-liquid separation technique and anaerobic fermentation technology, first excrement sewage is separated into argol and liquid dung, argol becomes fertilizer through processing, fertilizer can directly to farm crop, trees fertilising, liquid dung produces biogas and natural pond liquid through anaerobically fermenting, and biogas can be used for generating, natural pond liquid and can be used for pouring farmland and trees.
The utility model by being fixedly installed 6 water distribution laterals bottom the inlet channel of center, 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 the inlet channel of center from top to bottom, utilize the gravity of effluent sewage self, the drop of central duct height and the reducing effect of center water inlet pipe, effluent sewage enters in highly effective anaerobic reaction tank 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, liquid, admittedly carry out three-phase to be effectively separated, improve the comprehensive treatment effect of pig farm excrement dirt.
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 separately fixed on center inlet channel outer wall and highly effective anaerobic reaction top tank structure, be easier to the separation completely of solid, liquid, gas three-phase; And the top of the utility model highly effective anaerobic reaction tank is oval structure, there is not reaction Dead Core Problems in retort, facilitate liquids and gases to overturn mixing back and forth in anaerobic reaction tank, make reaction more thorough, separating effect is more thorough.
The difference of the dirty utilization system of excrement of the present utility model and general Waste Water Treatment is: not only excrement sewage is created biogas by fermentation, also have passed through solid-liquid separation, create fertilizer, and avoid the possibility that waste gas produces secondary pollution, make refuse reach recycling effectively fully, improve comprehensive utilization ratio.
Accompanying drawing illustrates:
Fig. 1 is one-piece construction principle schematic of the present utility model;
Fig. 2 is the structural representation of highly effective anaerobic reaction tank in Fig. 1;
Fig. 3 be in Fig. 2 fixed support and 6 water distribution laterals look up structural representation;
Fig. 4 is the structure for amplifying schematic diagram of reflection cone in Fig. 2.
Embodiment:
Below in conjunction with accompanying drawing, the utility model is further explained and illustrate:
See Fig. 1, the dirty integration treatment system of a kind of pig farm excrement, comprise excrement dirty collector unit, solid-liquid separation unit, anaerobically fermenting unit, biogas utilization unit and natural pond liquid range site, the dirty collector unit of excrement comprises filtering basin 2, stercoroma pond 3 and Buffer Pool 6, after the excrement sewage 1 ejected from pig house is filtered by filtering basin 2, waste liquid is drained in Buffer Pool 6, the dirt of solid excrement is transported in stercoroma pond 3; Solid-liquid separation unit comprises solid-liquid separating machine 4 and fertilizer treatment unit 5, the solid excrement soiled ends in stercoroma pond 3 cross solid-liquid separating machine 4 process after, solid matter carries out processing through fertilizer treatment unit 5, liquid flow in Buffer Pool 6; Anaerobically fermenting unit is highly effective anaerobic reaction tank 8, and the waste water in Buffer Pool 6 enters into highly effective anaerobic reaction tank 8 and carries out anaerobically fermenting process after lift pump 7 promotes; Biogas utilization unit comprises biogas cabinet 10, methane purifying device 11 and biogas electricity generation apparatus 12, highly effective anaerobic reaction tank 8 li of biogas produced enter in biogas cabinet 10 through getter pipeline 9, export the biogas come and be input in biogas electricity generation apparatus 12 after methane purifying device 11 purifies from biogas cabinet 10; Natural pond liquid range site comprises natural pond liquid storage pool 14, forestry irrigation rig 15 and farmland irrigating device 16, the natural pond liquid that 8 li, highly effective anaerobic reaction tank produces flows in natural pond liquid storage pool 14 through natural pond liquid transport pipe 13, as required, the natural pond liquid of natural pond liquid storage pool 14 flows into respectively in forestry irrigation rig 15 and farmland irrigating device 16 and utilizes.
See Fig. 2, Fig. 3 and Fig. 4, highly effective anaerobic reaction tank 8 central position is provided with center inlet channel 19, the height of center inlet channel 19 is 5/3 of highly effective anaerobic reaction tank 8 tank body height, center inlet channel 19 runs through highly effective anaerobic reaction tank 8, water distribution pipe 28 is fixedly installed by fixed support 27 bottom center inlet channel 19, water distribution pipe 28 is made up of 6 water distribution laterals, 6 water distribution laterals with bottom center inlet channel 19 for the center of circle is uniformly distributed, angle often between adjacent two water distribution laterals is 60 degree, a reflection cone 29 is provided with below the end of every root water distribution lateral, the cross section trilateral in obtuse angle of reflection cone 29, between sidepiece and bottom, angle is 30 degree, adapter bonnet 23 centered by center inlet channel 19 and highly effective anaerobic reaction tank 8 top institute contact position, center inlet channel 19 upper end one sidepiece is provided with inlet channel 17, the other side is provided with gas exhaust duct 20 and reflux line 22, inlet channel 17 is connected by the 6 water distribution laterals in center inlet channel 19 and bottom, highly effective anaerobic reaction tank 8 tip-end-side is provided with drainage pipeline 25, inside highly effective anaerobic reaction tank 8, upper position installs and is equipped with triphase separator 24, bottom highly effective anaerobic reaction tank 8, be provided with firm banking 31, above firm banking 31, be provided with sludge discharging port and observe manhole (not shown in FIG.), wherein: the height of giving vent to anger of gas exhaust duct 20 higher than the water inlet height of inlet channel 17, the water inlet height of inlet channel 17 higher than the drain height of the water inlet height bottom the freeboard on reflux line 22 top, reflux line 22 higher than drainage pipeline 25.
Fixed support 27 is made up of vertical supporting rod 30 and support rail 32, support rail 32 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, little regular hexagon is sleeved in large regular hexagon, and 6 water distribution laterals are fixedly welded on each summit of little regular hexagon and large regular hexagon formation respectively; A vertical supporting rod 30 is vertically provided with respectively at little regular hexagon and large regular hexagon each summit place, vertical supporting rod 30 has 12, length is consistent, and the top of 12 vertical supporting rods is welded on little regular hexagon respectively and large regular hexagon each summit place, bottom are welded on the firm banking 31 bottom highly effective anaerobic reaction tank 8.
Highly effective anaerobic reaction tank 8 top is oval structure, triphase separator 24 comprises triphase separator overhead gage and triphase separator lower shoe, triphase separator overhead gage and triphase separator lower shoe parallel to each other, triphase separator overhead gage upper end is fixed on the outer wall of center inlet channel 19, angle between triphase separator overhead gage upper end and center inlet channel 19 outer wall is 60 degree, the tapered distribution of triphase separator overhead gage; Triphase separator lower shoe lower end is fixed on the inwall of highly effective anaerobic reaction tank 8, and the angle between triphase separator lower shoe lower end and highly effective anaerobic reaction tank 8 inwall is 120 degree, and triphase separator lower shoe is annular distribution.Wherein: the water port of drainage pipeline 25 is positioned at the upper end of triphase separator 24.
Inlet channel 17 is provided with water inlet control valve door 18, gas exhaust duct 20 is provided with gas exhaust inspecting valve 21, drainage pipeline 25 is provided with draining control valve door 26.
The 6 piece water distribution laterals of the utility model by being fixedly installed bottom center inlet channel 19, the reflection cone 29 arranged below the end of every root water distribution lateral, inlet channel is connected with respective reflection cone with 6 water distribution laterals through after the inlet channel of center from top to bottom, utilize the gravity of effluent sewage self, the drop of central duct height and the reducing effect of center water inlet pipe, effluent sewage enters in highly effective anaerobic reaction tank 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, liquid, admittedly carry out three-phase to be effectively separated, improve the comprehensive treatment effect of pig farm excrement dirt.
Triphase separator 24 of the present utility model is easier to the separation completely of solid, liquid, gas three-phase, and the utility model highly effective anaerobic reaction tank 8 tank body top is set to oval structure, reaction Dead Core Problems is there is not in retort, liquids and gases are facilitated to overturn mixing back and forth in anaerobic reaction tank, make reaction more thorough, separating effect is more thorough.
Claims (4)
1. the dirty integration treatment system of pig farm excrement, comprise excrement dirty collector unit, solid-liquid separation unit, anaerobically fermenting unit, biogas utilization unit and natural pond liquid range site, the dirty collector unit of described excrement comprises filtering basin (2), stercoroma pond (3) and Buffer Pool (6), after the excrement sewage (1) ejected from pig house is filtered by filtering basin (2), waste liquid is drained in Buffer Pool (6), the dirt of solid excrement is transported in stercoroma pond (3), described solid-liquid separation unit comprises solid-liquid separating machine (4) and fertilizer treatment unit (5), and after the solid excrement soiled ends in described stercoroma pond (3) crosses solid-liquid separating machine (4) process, solid matter carries out processing through fertilizer treatment unit (5), liquid flow in described Buffer Pool (6), described anaerobically fermenting unit is highly effective anaerobic reaction tank (8), and the waste water in described Buffer Pool (6) enters into highly effective anaerobic reaction tank (8) and carries out anaerobically fermenting process after lift pump (7) promotes, described biogas utilization unit comprises biogas cabinet (10), methane purifying device (11) and biogas electricity generation apparatus (12), the biogas that described highly effective anaerobic reaction tank (8) is inner produced enters in described biogas cabinet (10) through getter pipeline (9), exports the biogas come and be input in biogas electricity generation apparatus (12) after methane purifying device (11) purification from biogas cabinet (10), described natural pond liquid range site comprises natural pond liquid storage pool (14), forestry irrigation rig (15) and farmland irrigating device (16), the natural pond liquid that described highly effective anaerobic reaction tank (8) is inner produced flows in natural pond liquid storage pool (14) through natural pond liquid transport pipe (13), as required, the natural pond liquid in natural pond liquid storage pool (14) flows into respectively in forestry irrigation rig (15) and farmland irrigating device (16) and utilizes, it is characterized in that: described highly effective anaerobic reaction tank (8) central position is provided with center inlet channel (19), the height at described center inlet channel (19) is 5/3 of described highly effective anaerobic reaction tank (8) tank body height, described highly effective anaerobic reaction tank (8) is run through at described center inlet channel (19), water distribution pipe (28) is fixedly installed by fixed support (27) in bottom, described center inlet channel (19), described water distribution pipe (28) is made up of 6 water distribution laterals, 6 water distribution laterals with bottom, described center inlet channel (19) for the center of circle is uniformly distributed, angle often between adjacent two water distribution laterals is 60 degree, a reflection cone (29) is provided with below the end of every root water distribution lateral, the cross section trilateral in obtuse angle of described reflection cone (29), between sidepiece and bottom, angle is 30 degree, adapter bonnet (23) centered by described center inlet channel (19) and described highly effective anaerobic reaction tank (8) top institute contact position, inlet channel (19) upper end one, described center sidepiece is provided with inlet channel (17), the other side is provided with gas exhaust duct (20) and reflux line (22), and described inlet channel (17) is connected by the 6 water distribution laterals in described center inlet channel (19) and bottom, described highly effective anaerobic reaction tank (8) tip-end-side is provided with drainage pipeline (25), described highly effective anaerobic reaction tank (8) the inside upper position installs and is equipped with triphase separator (24), described highly effective anaerobic reaction tank (8) bottom is provided with firm banking (31), and described firm banking (31) top is provided with sludge discharging port and observes manhole, the height of giving vent to anger of described gas exhaust duct (20) higher than the water inlet height of described inlet channel (17), the water inlet height of described inlet channel (17) higher than the water inlet height of the freeboard on described reflux line (22) top, described reflux line (22) bottom higher than the drain height of described drainage pipeline (25).
2. the dirty integration treatment system of pig farm according to claim 1 excrement, it is characterized in that: described fixed support (27) is made up of vertical supporting rod (30) and support rail (32), described support rail (32) 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 provided with a vertical supporting rod (30) respectively, described vertical supporting rod (30) is 12, length is consistent, and the top of 12 vertical supporting rods (30) is welded on described little regular hexagon respectively and described large regular hexagon each summit place, bottom are welded on the firm banking (31) of described highly effective anaerobic reaction tank (8) bottom.
3. the dirty integration treatment system of pig farm according to claim 2 excrement, it is characterized in that: described highly effective anaerobic reaction tank (8) top is oval structure, described triphase separator (24) 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 the outer wall at described center inlet channel (19), angle between described triphase separator overhead gage upper end and center inlet channel (19) outer wall is 60 degree, the tapered distribution of described triphase separator overhead gage, described triphase separator lower shoe lower end is fixed on the inwall of described highly effective anaerobic reaction tank (8), angle between described triphase separator lower shoe lower end and described highly effective anaerobic reaction tank (8) inwall is 120 degree, and described triphase separator lower shoe is annular distribution, the water port of described drainage pipeline (25) is positioned at the upper end of described triphase separator (24).
4. the dirty integration treatment system of pig farm according to claim 1 excrement, it is characterized in that: on described inlet channel (17), be provided with water inlet control valve door (18), described gas exhaust duct (20) is provided with gas exhaust inspecting valve (21), described drainage pipeline (25) is provided with draining control valve door (26).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520239950.XU CN204737845U (en) | 2015-04-21 | 2015-04-21 | Dirty wholeization processing system of pig farm excrement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520239950.XU CN204737845U (en) | 2015-04-21 | 2015-04-21 | Dirty wholeization processing system of pig farm excrement |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204737845U true CN204737845U (en) | 2015-11-04 |
Family
ID=54419590
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520239950.XU Active CN204737845U (en) | 2015-04-21 | 2015-04-21 | Dirty wholeization processing system of pig farm excrement |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204737845U (en) |
-
2015
- 2015-04-21 CN CN201520239950.XU patent/CN204737845U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104817170B (en) | Large-scale pig farm treatment for cow manure ecological recycle system | |
| CN104761104B (en) | Pig farm muck reprocessing resource cyclic utilization system | |
| CN102718355B (en) | Breeding pollution discharge treatment system and treatment method thereof | |
| CN102531293B (en) | Centralized treatment system for sewage in rural area | |
| CN104773922B (en) | Large-scale professional pig farm excrement dirt total system | |
| CN209039465U (en) | Anaerobic baffled circulation gas agitating black film biogas slurry reaction tank | |
| CN104710092A (en) | Plastic steel biogas septic tank | |
| CN105417893A (en) | Multiphase circulation integrated sewage treatment equipment | |
| CN103708674B (en) | A kind of ductwork type ight soil and organic sewage refuse disposal installation | |
| CN204644062U (en) | The dirty utilization system of aquaculture excrement | |
| CN204643958U (en) | Modernization pig house wastewater reuse approach anaerobic reaction system | |
| CN204644059U (en) | Pig farm muck reprocessing resource cyclic utilization system | |
| CN104787979A (en) | Comprehensive utilization system for feces in large-scale breeding industry | |
| CN205275425U (en) | Heterogeneous circulation integrative sewage treatment device | |
| CN202087572U (en) | Complete equipment used for resource recovery of kitchen garbage | |
| CN204737845U (en) | Dirty wholeization processing system of pig farm excrement | |
| CN204644066U (en) | Livestock culture industry waste water high-efficiency treatment unit | |
| CN207567067U (en) | A kind of pig farm circulatory system | |
| CN204224404U (en) | A kind of feces of farm treatment facility | |
| CN204644061U (en) | The dirty integrated high-efficiency treatment system of pig house excrement | |
| CN104860398A (en) | Intensive device for treating rural domestic sewage and construction method thereof | |
| CN202465457U (en) | Centralized processing system of sewage in rural areas | |
| CN204529451U (en) | Biogas septic tank | |
| CN205258257U (en) | Mud nature bio -concentration mummification pond suitable for low discharge sewage treatment system | |
| 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 |