CN202297327U - Biogas system for culture farm - Google Patents
Biogas system for culture farm Download PDFInfo
- Publication number
- CN202297327U CN202297327U CN201120394758XU CN201120394758U CN202297327U CN 202297327 U CN202297327 U CN 202297327U CN 201120394758X U CN201120394758X U CN 201120394758XU CN 201120394758 U CN201120394758 U CN 201120394758U CN 202297327 U CN202297327 U CN 202297327U
- Authority
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- China
- Prior art keywords
- biogas
- pipe
- pool
- communicated
- natural pond
- 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.)
- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
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- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a biogas system for a culture farm, wherein the biogas system for the culture farm mainly comprises a sewage collecting pool, a preparation pool, a sand sediment channel, a regulating pool, an integral reactor, a concentration pool, an organic processing chamber, a liquid storage pool, a biogas slurry pipe, a gas and water separator, a booster fan, a flame arrester, a biogas residue pipe and a feeding pipe, wherein the concentration pool is communicated with the integral reactor through the feeding pipe, the upper part of the concentration pool is communicated with the biogas slurry pipe, the bottom of the concentration pool is provided with a conveying pump, the inlet end of the biogas residue pipe is communicated with the outlet end of the conveying pump, the outlet end of the biogas residue pipe is connected with the inlet end of the organic processing chamber, and the outlet end of the organic processing chamber is communicated with the liquid storage pool. The biogas system has the advantages that materials such as domestic animal excrement and straws can be collected and treated, biogas is produced to be used by residents, meanwhile, biogas residues and biogas slurry can be primarily separated, the biogas slurry is separated and is conveyed to farmlands for irrigation, the biogas residues are conveyed into the gas and water separator for separation, and the biogas system belongs to an effective path for improving the rural environmental sanitation and developing the green planting industry and the culture industry.
Description
Technical field:
The utility model belongs to the methane engineering technology field, is specifically related to a kind of plant bionethanation system.
Background technology:
Biogas, its major ingredient is a methane, and methane is a kind of ideal geseous fuel, and its colorless and odorless and can burn after an amount of air mixed.The thermal value of every cubic metre of pure methane is 34000 kilojoules, and the thermal value of every cubic metre of biogas is about the 20800-23600 kilojoule.Promptly after 1 cubic metre of biogas perfect combustion, can produce and be equivalent to the heat that 0.7 kilogram of hard coal provides.Compare with other combustion gas, its capability of antidetonance is better, is a kind of good clean fuel.Biogas also can be made the fuel of oil engine and produce industrial chemicals such as methyl alcohol, Superlysoform, tetracol phenixin except that direct burning is used for cooking, oven dry agricultural byproducts, heating, illumination and gas welding etc.The feed liquid and the sediment of after the firedamp gas equipment fermentation, discharging; Contain more rich nutritive substance; Can be used as fertilizer and feed, biogas is reproducible clean energy, traditional biological mass-energy sources such as both alternative stalk, fuel wood; Also commercial energy resource such as alternative coal, and Energy efficiency is apparently higher than stalk, fuel wood, coal etc.
A complete biogas fermentation engineering, no matter its scale has all comprised following technical process: the aftertreatment of the collection of raw material, pre-treatment, fermentation unit (methane-generating pit), discharging and the purification of biogas and storage etc.; The discharging aftertreatment technology is meant in fermentation unit depleted natural pond liquid and the processing of natural pond slag after fermentation finishes, and at present, most of biogas engineerings are paid attention to not enough to this technology; Be the natural pond slag to be disposed to the farmland together with natural pond liquid do the fertilizer use mostly; Or directly emit, directly discharging waste resource directly is discharged into the farmland biogas residue and biogas liquid and mixes; The easy blocking pipeline, discharging is inconvenient.
The utility model content:
In sum, in order to overcome the deficiency of prior art problem, the utility model provides a kind of plant bionethanation system; Can material collection such as animal residue and stalk be handled, output biogas supplies the resident to use, and it is in the aftertreatment technology of discharging simultaneously; Can natural pond slag and natural pond liquid be carried out initial gross separation, most natural pond liquid is separated, be delivered to the farmland and water; The natural pond liquid of natural pond slag and few part is delivered in the solid-liquid separating machine; Separating completely, is the effective measure of improving rural environmental hygiene, the effective way of development green planting industry, aquaculture.
For solving the problems of the technologies described above, the technical scheme that the utility model adopts is:
A kind of plant bionethanation system; Wherein, Mainly comprise collection dirty pond, preparing pool, desilting canal, equalizing tank, integrated reactor, concentration basin, have between machining, liquid storing pool, natural pond liquid pipe, air water separator, booster fan, natural pond slag pipe and feed-pipe, the dirty pond of said collection, preparing pool, desilting canal, equalizing tank are communicated with through pipeline successively, the exit end of equalizing tank is communicated with the entrance end of integrated reactor through feed-pipe; First outlet of integrated reactor is through the entrance end UNICOM of natural pond liquid pipe and concentration basin; The outlet at bottom end of concentration basin is provided with natural pond slag pipe, and natural pond slag pipe is provided with transferpump, and the exit end of natural pond slag pipe is connected with the inlet end between machining is arranged; There is the exit end between machining to be communicated with the inlet end of liquid storing pool; Second outlet of integrated reactor is communicated with the inlet end of air water separator through pipeline, and the exit end of air water separator passes through pipeline and is communicated with the inlet end of booster fan, and the exit end of booster fan passes through pipeline and is communicated with the peasant household cooker.
The dirty pond import of described collection is provided with barrier.
Pipeline between dirty pond of described collection and the preparing pool is provided with sewage pump.
Feed-pipe between described equalizing tank and the integrated producer is provided with cutting pump.
Pipeline between described air water separator and the booster fan is provided with digester.
Also be provided with spark arrester on the pipeline between described booster fan and the peasant household's cooker.
The beneficial effect of the utility model is:
1, the utility model uses in the aftertreatment technology of discharging; Natural pond slag and natural pond liquid are carried out initial gross separation; Most natural pond liquid is separated, be delivered to the farmland and water, the natural pond liquid that the natural pond slag is reached few part is delivered in the solid-liquid separating machine; Separate completely, thus the deficiency of avoiding natural pond slag and natural pond liquid to discharge together.
2, the utility model is simple in structure, performance is safe and reliable, long service life, can effectively assist solid-liquid separating machine that natural pond liquid and natural pond slag are thoroughly separated, and isolating natural pond liquid is used to water the farmland, and the natural pond slag then is used to make organic fertilizer.
Description of drawings:
Fig. 1 is the schema of the utility model.
Embodiment:
Below in conjunction with accompanying drawing the utility model is done further to specify.
As shown in Figure 1, a kind of plant bionethanation system, wherein; Mainly comprise collection dirty pond, preparing pool, desilting canal, equalizing tank, integrated reactor, concentration basin, have between machining, liquid storing pool, natural pond liquid pipe, air water separator, booster fan, natural pond slag pipe and feed-pipe; Wherein, collect dirty pond, preparing pool, desilting canal and equalizing tank and be communicated with successively through pipeline, the exit end of equalizing tank is communicated with the entrance end of integrated reactor through feed-pipe; First outlet of integrated reactor is through the entrance end UNICOM of natural pond liquid pipe and concentration basin; The outlet at bottom end of concentration basin is provided with natural pond slag pipe, and natural pond slag pipe is provided with transferpump, and the exit end of natural pond slag pipe is connected with the inlet end between machining is arranged; There is the exit end between machining to be communicated with the inlet end of liquid storing pool; Second outlet of integrated reactor is communicated with the inlet end of air water separator through pipeline, and the exit end of air water separator passes through pipeline and is communicated with the inlet end of booster fan, and the exit end of booster fan passes through pipeline and is communicated with the peasant household cooker.
The dirty pond import of described collection is provided with barrier.
Pipeline between dirty pond of described collection and the preparing pool is provided with sewage pump.
Feed-pipe between described equalizing tank and the integrated producer is provided with cutting pump.
Pipeline between described air water separator and the booster fan is provided with digester.
Also be provided with spark arrester on the pipeline between described booster fan and the peasant household's cooker.
During use, after flushing waste water and animal residue pass through the bigger swimmer of grid amputation, get into the dirty pond of collection and store; Be lifted into preparing pool through sewage pump and transfer excrement, stirrer is arranged in the preparing pool, through the homogeneous material of stirrer stirring; From flowing to equalizing tank, pump into integrated reactor through cutting pump through the desilting canal then, after the anaerobic digestion in the integrated reactor; The biogas that produces is stored in the flexible gas holder at integrated reactor top, and the gas after the moisture separator aqueous vapor is separated gets into the digester desulfurization, and the gas after desulfurization is through the booster fan supercharging; The spark arrester back-fire relief is supplied to peasant household's cooker, simultaneously; The natural pond slag that produces, natural pond liquid concentrate from flowing into concentration basin, and the transferpump through the concentration basin bottom has been delivered between machining then, natural pond slag, natural pond liquid in having between machining after solid-liquid separation; The natural pond slag is retained and is produced fertilizer, and natural pond liquid is from flowing in the liquid storing pool, in order to the irrigated farmland.
Claims (6)
1. plant's bionethanation system; It is characterized in that: mainly comprise collection dirty pond, preparing pool, desilting canal, equalizing tank, integrated reactor, concentration basin, have between machining, liquid storing pool, natural pond liquid pipe, air water separator, booster fan, natural pond slag pipe and feed-pipe; The dirty pond of said collection, preparing pool, desilting canal, equalizing tank are communicated with through pipeline successively; The exit end of equalizing tank is communicated with the entrance end of integrated reactor through feed-pipe, and first outlet of integrated reactor is through the entrance end UNICOM of natural pond liquid pipe and concentration basin, and the outlet at bottom end of concentration basin is provided with natural pond slag pipe; Natural pond slag pipe is provided with transferpump; The exit end of natural pond slag pipe is connected with the inlet end between machining is arranged, and has the exit end between machining to be communicated with the inlet end of liquid storing pool, and second outlet of integrated reactor is communicated with the inlet end of air water separator through pipeline; The exit end of air water separator is communicated with the inlet end of booster fan through pipeline, and the exit end of booster fan passes through pipeline and is communicated with the peasant household cooker.
2. a kind of plant according to claim 1 bionethanation system is characterized in that: the dirty pond import of described collection is provided with barrier.
3. a kind of plant according to claim 1 bionethanation system is characterized in that: the pipeline between dirty pond of described collection and the preparing pool is provided with sewage pump.
4. a kind of plant according to claim 1 bionethanation system is characterized in that: the feed-pipe between described equalizing tank and the integrated producer is provided with cutting pump.
5. a kind of plant according to claim 1 bionethanation system, it is characterized in that: the pipeline between described air water separator and the booster fan is provided with digester.
6. a kind of plant according to claim 1 bionethanation system is characterized in that: also be provided with spark arrester on the pipeline between described booster fan and the peasant household's cooker.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120394758XU CN202297327U (en) | 2011-10-17 | 2011-10-17 | Biogas system for culture farm |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120394758XU CN202297327U (en) | 2011-10-17 | 2011-10-17 | Biogas system for culture farm |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202297327U true CN202297327U (en) | 2012-07-04 |
Family
ID=46366265
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120394758XU Expired - Fee Related CN202297327U (en) | 2011-10-17 | 2011-10-17 | Biogas system for culture farm |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202297327U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103195271A (en) * | 2013-04-09 | 2013-07-10 | 山东佳源农牧科技发展有限公司 | Comprehensive planting and cultivation circulating system and method |
-
2011
- 2011-10-17 CN CN201120394758XU patent/CN202297327U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103195271A (en) * | 2013-04-09 | 2013-07-10 | 山东佳源农牧科技发展有限公司 | Comprehensive planting and cultivation circulating system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120704 Termination date: 20121017 |