CN204211738U - Biogas produces gathering system continuously - Google Patents
Biogas produces gathering system continuously Download PDFInfo
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- CN204211738U CN204211738U CN201420685514.0U CN201420685514U CN204211738U CN 204211738 U CN204211738 U CN 204211738U CN 201420685514 U CN201420685514 U CN 201420685514U CN 204211738 U CN204211738 U CN 204211738U
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- biogas
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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
- 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
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Abstract
The utility model aims to provide a kind ofly can produce biogas continuously, pollution-free, that resource utilization is high biogas produces gathering system continuously; It comprises its feed-water end via the water inlet pipe IC reactor, knockout drum, gas-holder, the liquid collection bath that are communicated with corresponding to source of sewage; Also liquid pump is provided with at the feed-water end place of described IC reactor; On described gas-holder, correspondence offers inlet mouth and air outlet, and is also provided with air outlet valve at the air outlet place of described gas-holder; The outlet side of described IC reactor is communicated with via collection tube is corresponding with the air inlet port of described knockout drum, and the air outlet of described knockout drum is via pneumatic tube and described gas-holder.
Description
Technical field
The utility model relates to methane producing apparatus field, particularly relates to a kind of biogas and produces gathering system continuously.
Background technology
Biogas, be various organic substance at isolated air, and under suitable temperature, pH value, through a kind of combustible gas that the fermentative action of microorganism produces, it belongs to secondary energy, and is renewable energy source.Meanwhile, biogas is also a kind of mixed gas, can burn, and is the mixture of multiple gases, and general containing methane 50 ~ 70%, all the other are carbonic acid gas and a small amount of nitrogen, hydrogen and hydrogen sulfide etc., and its characteristic is similar to Sweet natural gas.Biogas is used for cooking except direct burning, dries except agricultural byproducts, heating, illumination and gas welding etc., also can make the industrial chemicals such as the fuel of oil engine and methanol, formalin, tetracol phenixin.Current Gas application is more in vast Rural areas, and its aerogenesis mode is more adopt methane-generating pit, and in conjunction with animal excrement etc. to produce biogas, and in it uses, the biogas which produces can not effectively persistence produce, and meanwhile, its usability is single, and for some enterprises, it is particularly the industrial enterprise of raw material with agricultural byproducts, aforesaid way can not well be applied, and can not aerogenesis be continued, a large amount of sewage can be produced in its application process simultaneously, and IC reactor is in the market a kind of well conversion unit, how prior art is combined better with IC reactor, and be applied in biogas and go, the production cost of enterprise is reduced, simultaneously free from environmental pollution again, improve the utilization ratio of resource, realize the recycle of resource, just become the direction that enterprise and governments at all levels will make great efforts to probe in Gas application.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, adapts to reality need, provides a kind of and can produce biogas continuously, pollution-free, that resource utilization is high biogas produces gathering system continuously.
In order to realize the purpose of this utility model, the technical scheme that the utility model adopts is:
Design a kind of biogas and produce gathering system continuously, it comprises its feed-water end via the water inlet pipe IC reactor, knockout drum, gas-holder, the liquid collection bath that are communicated with corresponding to source of sewage; Also liquid pump is provided with at the feed-water end place of described IC reactor; On described gas-holder, correspondence offers inlet mouth and air outlet, and is also provided with air outlet valve at the air outlet place of described gas-holder; The outlet side of described IC reactor is communicated with via collection tube is corresponding with the air inlet port of described knockout drum, the air outlet of described knockout drum is communicated with via pneumatic tube is corresponding with the inlet mouth of described gas-holder, and the rising pipe of described IC reactor is corresponding with described liquid collection bath to be communicated with.
Further, the bleed port place of described knockout drum lower end is provided with tapping valve, described tapping valve is also corresponding with described liquid collection bath to be communicated with.
Further, off-gas pump is provided with at described IC reactor with also corresponding on the collection tube between described knockout drum.
Further, also correspondingly on the pneumatic tube between described knockout drum with described gas-holder topping-up pump is provided with.
Further, on described gas-holder, also correspondence is provided with purge valve.
Further, on described gas-holder, also correspondence is provided with tensimeter.
Further, described gas-holder is spherical.
The beneficial effects of the utility model are:
1. by system designed by the utility model, can carry out Collection utilization to sewage, and to produce biogas, the biogas simultaneously after native system process directly by utilize, also can be able to store, in order to use; Native system can continuous print Biogas to adopt the maximum benefit of native system to be, and not by the restriction of other condition, simultaneously, adopt native system can also carry out effective recycle to existing resource, save the energy, native system is pollution-free when applying simultaneously, saves the energy, meets the requirement of national sustainable development.
2. native system also have occupation of land less, organic loading high, impact resistance, anti-seismic design be strong, the advantages such as stable performance, operational administrative are simple, energy-conserving and environment-protective.
3. the utility model also has other advantages and structure corresponding is in an embodiment proposed in the lump.
Accompanying drawing explanation
Fig. 1 is the utility model cardinal principle schematic diagram;
The IC reactor primary structure that Fig. 2 uses for the utility model illustrates schematic diagram;
In figure: 1. water inlet pipe; 2.IC reactor; 3. downtake; 4. primary separator; 5. riser tube; 6. second-stage separator; 7. overflow weir; The knockout drum of 8.IC reactor; 9. rising pipe; 10. collection tube; 11. knockout drums; 12. gas-holder; 13. liquid pumps; 14. off-gas pumps; 15. pneumatic tubes; 16. topping-up pumps; 17. air outlet valves; 18. tapping valves; 19. purge valves; 20. tensimeters; 21. liquid collection bath.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated:
Embodiment 1: a kind of biogas produces gathering system continuously, see Fig. 1, Fig. 2; It comprises its feed-water end via the water inlet pipe 1 IC reactor 2, knockout drum 11, gas-holder 12, the liquid collection bath 21 that are communicated with corresponding to source of sewage; Liquid pump 13 is also provided with at the feed-water end place of IC reactor 2; On described gas-holder 12, correspondence offers inlet mouth and air outlet, and is also provided with air outlet valve 17 at the air outlet place of gas-holder; The outlet side of described IC reactor 2 is communicated with via collection tube 10 is corresponding with the air inlet port of described knockout drum 11, the air outlet of described knockout drum 11 is communicated with via pneumatic tube 15 is corresponding with the inlet mouth of described gas-holder 12, and the rising pipe 9 of described IC reactor 2 is corresponding with described liquid collection bath 21 to be communicated with.Meanwhile, be also provided with tapping valve 18 at the bleed port place of described knockout drum 11 lower end, described tapping valve 18 is also corresponding with described liquid collection bath 21 to be communicated with, and uses in isolated for knockout drum liquid collecting to liquid collection bath with this in order to it.Further, also correspondingly on the collection tube 10 between IC reactor 2 with described knockout drum 11 be provided with off-gas pump 14, other that IC reactor can be produced by this off-gas pump are effectively drawn, and are delivered in knockout drum, improve the efficiency of native system.Meanwhile, also correspondingly on the pneumatic tube and between knockout drum 11 with described gas-holder 12 topping-up pump 16 is provided with.In order to improve security and the stability of native system, on described gas-holder 12, also correspondence is provided with purge valve 19.Meanwhile, on described gas-holder 12, also correspondence is provided with tensimeter 20, and as shown in the figure, described gas-holder 12 is spherical.
Understand for ease of illustrating, in conjunction with native system, the present embodiment is by 2 as follows to its principles and methods by reference to the accompanying drawings to used IC reactor:
Sewage to be pumped in IC reactor 2 by liquid pump 13 that hybrid concurrency is raw effectively forms anaerobic reaction with the granule sludge in this IC reactor by water inlet pipe 1, and sewage is under high concentration sludge effect, and the most of organism in it is converted into biogas.After being converted into biogas, the mixed solution upstream of generation and the violent disturbance of biogas to make in this IC reactor in reaction zone that mud is in expanding and fluidized state, and strengthen muddy water surface contact with this, meanwhile, mud also maintains high activity thus.Along with increasing of biogas output, part mud mixture is separated to primary separator 4 by biogas-lift, solid-liquid after primary separator process freely falls, and part mud mixture is continued to rise in secondary mixing zone by biogas and carries out anaerobic reaction, again effectively be separated by second-stage separator 6, simultaneously, to be transported to by riser tube 5 through the isolated biogas of primary separator 4 in the knockout drum 8 of IC reactor and to be separated, liquid after separation is fallen by the downtake 3 in IC reactor, processed water to flow into rising pipe 9 by overflow weir 7 and flow out into liquid collection bath, and to be delivered in knockout drum 11 by collection tube 10 and through off-gas pump via the biogas after the knockout drum 8 of IC reactor is separated and to be again separated, improve its purity, high density biogas after separation is pressurized in pump delivery to gas-holder and uses for gas equipment.
Although; what embodiment of the present utility model was announced is preferred embodiment; but be not limited thereto; those of ordinary skill in the art; very easily according to above-described embodiment, understand spirit of the present utility model, and make different amplifications and change; but only otherwise depart from spirit of the present utility model, all in protection domain of the present utility model.
Claims (7)
1. biogas produces a gathering system continuously, it is characterized in that: it comprises its feed-water end via water inlet pipe (1) the IC reactor (2), knockout drum (11), gas-holder (12), the liquid collection bath (21) that are communicated with corresponding to source of sewage; Liquid pump (13) is also provided with at the feed-water end place of described IC reactor (2); Offer inlet mouth and air outlet in the upper correspondence of described gas-holder (12), and be also provided with air outlet valve (17) at the air outlet place of described gas-holder; The outlet side of described IC reactor (2) is communicated with via collection tube (10) is corresponding with the air inlet port of described knockout drum (11), the air outlet of described knockout drum (11) is communicated with via pneumatic tube (15) is corresponding with the inlet mouth of described gas-holder (12), and the rising pipe (9) of described IC reactor (2) is corresponding with described liquid collection bath (21) to be communicated with.
2. biogas as claimed in claim 1 produces gathering system continuously, and it is characterized in that: the bleed port place of described knockout drum (11) lower end is provided with tapping valve (18), described tapping valve (18) is also corresponding with described liquid collection bath (21) to be communicated with.
3. biogas as claimed in claim 1 produces gathering system continuously, it is characterized in that: go up at described IC reactor (2) and the collection tube (10) between described knockout drum (11) and be also correspondingly provided with off-gas pump (14).
4. biogas as claimed in claim 1 produces gathering system continuously, it is characterized in that: also correspondingly on the pneumatic tube between described knockout drum (11) with described gas-holder (12) be provided with topping-up pump (16).
5. biogas as claimed in claim 1 produces gathering system continuously, it is characterized in that: the upper also correspondence of described gas-holder (12) is provided with purge valve (19).
6. biogas as claimed in claim 1 produces gathering system continuously, it is characterized in that: the upper also correspondence of described gas-holder (12) is provided with tensimeter (20).
7. biogas as claimed in claim 1 produces gathering system continuously, it is characterized in that: described gas-holder (12) is for spherical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420685514.0U CN204211738U (en) | 2014-11-17 | 2014-11-17 | Biogas produces gathering system continuously |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420685514.0U CN204211738U (en) | 2014-11-17 | 2014-11-17 | Biogas produces gathering system continuously |
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| Publication Number | Publication Date |
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| CN204211738U true CN204211738U (en) | 2015-03-18 |
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| CN201420685514.0U Active CN204211738U (en) | 2014-11-17 | 2014-11-17 | Biogas produces gathering system continuously |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107061985A (en) * | 2017-05-23 | 2017-08-18 | 河南美丽乡村环保科技有限公司 | Gas-liquid separation low pressure caisson |
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2014
- 2014-11-17 CN CN201420685514.0U patent/CN204211738U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107061985A (en) * | 2017-05-23 | 2017-08-18 | 河南美丽乡村环保科技有限公司 | Gas-liquid separation low pressure caisson |
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| GR01 | Patent grant |