CN104357318A - Integrated sedimentation/fermentation biogas device - Google Patents
Integrated sedimentation/fermentation biogas device Download PDFInfo
- Publication number
- CN104357318A CN104357318A CN201410646929.1A CN201410646929A CN104357318A CN 104357318 A CN104357318 A CN 104357318A CN 201410646929 A CN201410646929 A CN 201410646929A CN 104357318 A CN104357318 A CN 104357318A
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- China
- Prior art keywords
- sweathouse
- fermentation
- settling tank
- biogas
- room
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/36—Means for collection or storage of gas; Gas holders
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/58—Reaction vessels connected in series or in parallel
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/12—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus by pressure
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M45/00—Means for pre-treatment of biological substances
- C12M45/04—Phase separators; Separation of non fermentable material; Fractionation
Abstract
The invention discloses an integrated sedimentation/fermentation biogas device and belongs to the field of energy. The integrated sedimentation/fermentation biogas device comprises a sedimentation tank (1), a fermentation room (3), an overflow room (5) and a liquid storage tank (6) which are sequentially connected, wherein the sedimentation tank (1) is connected with the fermentation room (3) by virtue of a feed pipe (9), the upper part of the fermentation room (3) is a biogas chamber (11) which is connected with a biogas-guide pipe (4), the lower part of the fermentation room (3) is connected with the overflow room (5) by virtue of a fermentation broth channel (10) and the overflow room (5) is connected with the liquid storage tank (6) by virtue of an overflow opening (12). By the integrated sedimentation/fermentation biogas device, such technical problems of the existing biogas tank as difficult discharge of sediment slag and interruption of a fermentation process are solved and the integrated sedimentation/fermentation biogas device disclosed by the invention has the advantages of complete pretreatment and sedimentation, continuous and stable fermentation process, no need of discharging of a large quantity of materials in the fermentation room, high yield of biogas, large biogas storage space and zero energy consumption during the treatment process.
Description
Technical field
The invention belongs to energy field, be specifically related to a kind of precipitation fermentation integral type firedamp gas equipment.
Background technology
Existing domestic methane tank is traditional hydraulic type biomass pool, and fermentation raw material does not have acidified, precipitation process, directly enters methane-generating pit, sediment is deposited on bottom methane-generating pit, and after running for some time, sediment occupies fermenting space, discharging difficulty, factor of created gase reduces, and result of use is not good.Existing middle-size and small-size biogas engineering is that domestic methane tank amplifies or builds an airtight tank body, separately build gas storage holder, all there is fermentation vat sediment many, discharging difficulty, fermentation is not thorough, and result of use can not continue the problems such as maintenance, after running for some time, need to interrupt fermenting process and just can carry out large discharging, then just can restart operation.
Summary of the invention
The object of the invention is to there is sediment discharging difficulty to solve existing methane-generating pit, need the technical barrier interrupting fermenting process, for people provide a kind of fermenting process continual and steady, sweathouse is without the need to large discharging, factor of created gase is high, air storage space is large, the precipitation fermentation integral type firedamp gas equipment that treating processes zero consumes energy.
The object of the invention is to be realized by following proposal.
Precipitation fermentation integral type firedamp gas equipment of the present invention, it is characterized in that described precipitation fermentation integral type firedamp gas equipment by between settling tank, sweathouse, discharge and liquid storage tank connect and compose successively, wherein, settling tank is connected with sweathouse by feed-pipe, sweathouse top is air chamber, air chamber is connected with airway, and sweathouse bottom is connected with between discharge by fermented liquid passage, is connected between discharge by liquid spill-way with liquid storage tank.
In such scheme, described settling tank is simple sedimentation pond or multifeed clarifier, and in multifeed clarifier, previous stage settling tank is connected with rear stage settling tank by feed liquid passage, and last step settling tank is connected with sweathouse by feed-pipe.
In such scheme, described sweathouse is single-stage sweathouse or multistage sweathouse, and in multistage sweathouse, previous stage sweathouse is connected with rear stage sweathouse by fermented liquid passage, and last step sweathouse is connected with between discharge by fermented liquid passage.
In such scheme, between described settling tank, discharge and the top of liquid storage tank is separately installed with removable cover.
In such scheme, described feed-pipe is from the horizontal by 45 ° of inclination angles.
Present invention employs settling tank (can be multistage as required) to process fermented feed liquid, by action of gravity, sediment deposits at the bottom of settling tank, and the feed liquid through preliminary acidifying, precipitation enters sweathouse (can be multistage as required) fermentation by feed-pipe.The biogas produced after fermentation is stored in air chamber, and along with methane quantity increases, biogas pressure increases, and by the feed liquid in sweathouse by between fermented liquid passage press-in discharge, the liquid level between discharge rises to liquid spill-way, finally flows into liquid storage tank.
The present invention utilizes gravity effectively to remove sediment, reduces the TS(total solids of feed liquid) concentration, alleviate aftertreatment pressure, sweathouse is without the need to interrupting the large discharging of fermentation, and large discharging completes in settling tank, ensure that the continuous service of methane-generating pit.Inclination angle is that the feed-pipe of 45 ° connects the middle part of settling tank and the bottom of sweathouse, achieves the function of waterpower plug-flow and stirring, after feed liquid is thoroughly fermented by sweathouse, discharges under biogas pressure effect, finally overflow to discharge pond.
In sum, the invention solves existing methane-generating pit and there is sediment discharging difficulty, need the technical barrier interrupting fermenting process, the precipitation fermentation integral type firedamp gas equipment pre-treatment precipitation provided for people is thorough, fermenting process is continual and steady, and sweathouse is without the need to large discharging, and factor of created gase is high, air storage space is large, and treating processes zero consumes energy.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present invention.
In figure: 1. settling tank; 2. sediment; 3. sweathouse; 4. airway; 5. between discharge; 6. liquid storage tank; 7. removable cover; 8. feed liquid passage; 9. feed-pipe; 10. fermented liquid passage; 11. air chambers; 12. liquid spill-ways.
Embodiment
The invention is further illustrated by the following examples, and the present invention is not limited only to described embodiment.
Embodiment one
The precipitation fermentation integral type firedamp gas equipment of this example, by between simple sedimentation pond 1, single-stage sweathouse 3, discharge 5 and liquid storage tank 6 connect and compose successively, wherein, the middle part of settling tank 1 is connected with bottom sweathouse 3 by feed-pipe 9, sweathouse 3 top is air chamber 11, air chamber 11 is connected with airway 4, and sweathouse 3 bottom is connected in the middle part of 5 with between discharge by fermented liquid path 10, and between discharge, 5 tops are connected with liquid storage tank 6 by liquid spill-way 12.
Between settling tank 1, discharge 5 and the top of liquid storage tank 6 be separately installed with removable cover 7, prevent people and animals from falling into.
Feed-pipe 9 is from the horizontal by 45 ° of inclination angles.
Biogas in air chamber 11 is derived by airway 4 and is used.
The precipitation fermentation integral type firedamp gas equipment of this example is applicable to the commercialized biogas digester of the material such as glass reinforced plastic, plastics that anaerobically fermenting total pond appearance is 50-300m3, or the biogas engineering of steel and concrete structure, for subterranean tunnel formula methane-generating pit, save space and cost, achieve gravity flow charging, hydraulic mixing, waterpower plug-flow, feed liquid overflow, whole treating processes is without the need to consumption of power.
Embodiment two
The precipitation fermentation integral type firedamp gas equipment of this example as shown in Figure 1, except settling tank 1 is two-stage settling tank, sweathouse 3 is between two-stage fermentation, be connected with in the middle part of the settling tank of the second stage by feed liquid passage 8 in the middle part of first step settling tank, the middle part of second stage settling tank is connected with the bottom of first step sweathouse by feed-pipe 9, first step sweathouse bottom is connected with in the middle part of the sweathouse of the second stage by fermented liquid path 10, outside sweathouse bottom, the second stage to be connected in the middle part of 5 with between discharge by fermented liquid path 10, all the other are with embodiment one.
Embodiment three
The precipitation fermentation integral type firedamp gas equipment of this example, except settling tank 1 is two-stage settling tank, be connected with in the middle part of the settling tank of the second stage by feed liquid passage 8 in the middle part of first step settling tank, outside passing through feed-pipe 9 and be connected bottom sweathouse in the middle part of the settling tank of the second stage, all the other are with embodiment one.
Embodiment four
The precipitation fermentation integral type firedamp gas equipment of this example, except settling tank 1 is three grades of settling tanks, be connected with in the middle part of the settling tank of the second stage by feed liquid passage 8 in the middle part of first step settling tank, be connected with in the middle part of third stage settling tank by feed liquid passage 8 in the middle part of the settling tank of the second stage, outside passing through feed-pipe 9 and be connected bottom first step sweathouse in the middle part of third stage settling tank, all the other are with embodiment two.
Claims (5)
1. a precipitation fermentation integral type firedamp gas equipment, it is characterized in that described precipitation fermentation integral type firedamp gas equipment is connected and composed successively by (5) and liquid storage tank (6) between settling tank (1), sweathouse (3), discharge, wherein, settling tank (1) is connected with sweathouse (3) by feed-pipe (9), sweathouse (3) top is air chamber (11), air chamber (11) is connected with airway (4), sweathouse (3) bottom is connected with (5) between discharge by fermented liquid passage (10), and between discharge, (5) are connected with liquid storage tank (6) by liquid spill-way (12).
2. precipitate fermentation integral type firedamp gas equipment according to claim 1, it is characterized in that described settling tank (1) is for simple sedimentation pond or multifeed clarifier, in multifeed clarifier, previous stage settling tank is connected with rear stage settling tank by feed liquid passage (8), and last step settling tank is connected with sweathouse (3) by feed-pipe (9).
3. precipitate fermentation integral type firedamp gas equipment according to claim 1, it is characterized in that described sweathouse (3) is for single-stage sweathouse or multistage sweathouse, in multistage sweathouse, previous stage sweathouse is connected with rear stage sweathouse by fermented liquid passage (10), and last step sweathouse is connected with (5) between discharge by fermented liquid passage (10).
4. precipitate fermentation integral type firedamp gas equipment according to claim 1, it is characterized in that the top of (5) and liquid storage tank (6) between described settling tank (1), discharge is separately installed with removable cover (7).
5. precipitate fermentation integral type firedamp gas equipment according to claim 1, it is characterized in that described feed-pipe (9) is from the horizontal by 45 ° of inclination angles.
Priority Applications (1)
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CN201410646929.1A CN104357318A (en) | 2014-11-16 | 2014-11-16 | Integrated sedimentation/fermentation biogas device |
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CN201410646929.1A CN104357318A (en) | 2014-11-16 | 2014-11-16 | Integrated sedimentation/fermentation biogas device |
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CN104357318A true CN104357318A (en) | 2015-02-18 |
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CN201410646929.1A Pending CN104357318A (en) | 2014-11-16 | 2014-11-16 | Integrated sedimentation/fermentation biogas device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104928158A (en) * | 2015-06-25 | 2015-09-23 | 南安市绿野沼气技术开发研究所 | Sedimentation and fermentation integrated biogas generator |
CN106045591A (en) * | 2016-06-06 | 2016-10-26 | 区登波 | Organic fertilizer fermentation method with silkworm excrement as main raw material |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2697088Y (en) * | 2004-04-17 | 2005-05-04 | 吕军萍 | High-efficoient convenient methane-generating pit |
CN2793067Y (en) * | 2005-03-11 | 2006-07-05 | 胡志学 | Marsh gas pool with high yield |
CN201634676U (en) * | 2010-04-21 | 2010-11-17 | 广西壮族自治区林业科学研究院 | Tank type methane fermenting pool |
CN102634446A (en) * | 2012-05-04 | 2012-08-15 | 郑毅 | High-concentration position pressure type self-slagging methane generating pond |
CN203474793U (en) * | 2013-08-19 | 2014-03-12 | 吴海彪 | Novel water pressure type automatic circulation biogas digester |
-
2014
- 2014-11-16 CN CN201410646929.1A patent/CN104357318A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2697088Y (en) * | 2004-04-17 | 2005-05-04 | 吕军萍 | High-efficoient convenient methane-generating pit |
CN2793067Y (en) * | 2005-03-11 | 2006-07-05 | 胡志学 | Marsh gas pool with high yield |
CN201634676U (en) * | 2010-04-21 | 2010-11-17 | 广西壮族自治区林业科学研究院 | Tank type methane fermenting pool |
CN102634446A (en) * | 2012-05-04 | 2012-08-15 | 郑毅 | High-concentration position pressure type self-slagging methane generating pond |
CN203474793U (en) * | 2013-08-19 | 2014-03-12 | 吴海彪 | Novel water pressure type automatic circulation biogas digester |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104928158A (en) * | 2015-06-25 | 2015-09-23 | 南安市绿野沼气技术开发研究所 | Sedimentation and fermentation integrated biogas generator |
CN104928158B (en) * | 2015-06-25 | 2018-02-13 | 南安市绿野沼气技术开发研究所 | One kind precipitation fermentation integrated methane generating means |
CN106045591A (en) * | 2016-06-06 | 2016-10-26 | 区登波 | Organic fertilizer fermentation method with silkworm excrement as main raw material |
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Application publication date: 20150218 |