CN105505751A - Horizontal type plastic-steel super-long biogas tank - Google Patents
Horizontal type plastic-steel super-long biogas tank Download PDFInfo
- Publication number
- CN105505751A CN105505751A CN201610124010.5A CN201610124010A CN105505751A CN 105505751 A CN105505751 A CN 105505751A CN 201610124010 A CN201610124010 A CN 201610124010A CN 105505751 A CN105505751 A CN 105505751A
- Authority
- CN
- China
- Prior art keywords
- tank
- fermentor tank
- tank body
- stage
- fermentation tank
- 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.)
- Pending
Links
Classifications
-
- 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
-
- 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
-
- 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/20—Heat exchange systems, e.g. heat jackets or outer envelopes the heat transfer medium being a gas
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/24—Heat exchange systems, e.g. heat jackets or outer envelopes inside the vessel
-
- 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
Landscapes
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Zoology (AREA)
- Genetics & Genomics (AREA)
- Biochemistry (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Molecular Biology (AREA)
- Clinical Laboratory Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a horizontal type plastic-steel super-long biogas tank which comprises fermentation tanks. The fermentation tanks include multiple stages of fermentation tank bodies, wherein the first-stage fermentation tank body is connected with the second-stage fermentation tank body, the second-stage fermentation tank body is connected with the third-stage fermentation tank body, and the like; the multiple stages of fermentation tank bodies are communicated through ports in the lower portions of the walls of the fermentation tank bodies, a feeding pipe extending into the lower portion of the tank body is arranged on the first-stage fermentation tank body, a discharge pipe extending out of the lower portion of the tank body is arranged on the last-stage fermentation tank body, a gas outlet extending out of the top is formed in each stage of fermentation tank body, a temperature rising pressure pipe extending into the bottom of the tank body is further arranged on the first-stage fermentation tank body, the temperature rising pressure pipe horizontally extends from the bottom of the first-stage fermentation tank body to the bottom of the last but one stage of fermentation tank body in a communicating manner, upward gas nozzles which are evenly distributed are formed in the communicating part of the temperature rising pressure pipe, and a temperature rising water supply pipe extending into the lower portion of the tank body is further arranged on the last stage of fermentation tank body. The horizontal type plastic-steel super-long biogas tank has the advantages that multistage biogas fermentation is used, and the biogas tank is clean, environmental friendly, high in biogas utilization rate, and capable of saving resources and avoiding waste.
Description
Technical field:
The present invention relates to firedamp gas equipment, be specially a kind of horizontal plastic-steel overlength tank for sewage gas.
Background technology:
At present, the biogas room (pond) of the many traditional structures of China, be all be built into underground with soil, stone, mixed earth, permanent due to the time, to add external environment and geologic condition change, easily causes fermentation seepage, changes the situations such as excrement defunctionalization; Further, traditional biogas room (pond) all adopts one-level natural pond mode, and utilization ratio, the extracted amount of biogas are no more than 30%, about has the renewable energy resources of 70% not utilized, and waste is serious.
Summary of the invention:
For the deficiencies in the prior art, technical problem to be solved by this invention proposes the horizontal plastic-steel overlength tank for sewage gas that a kind of natural pondization is thorough, biogas utilization rate is high.
The horizontal plastic-steel overlength tank for sewage gas that can solve the problems of the technologies described above, its technical scheme comprises fermentor tank, difference is that described fermentor tank comprises multistage fermentor tank, in the horizontal direction, first step fermentor tank is coaxially connected with second stage fermentor tank, second stage fermentor tank is coaxially connected with third stage fermentor tank, by that analogy, be communicated with by the port of tank skin bottom between fermentor tank at different levels, first step fermentor tank is provided with the feed-pipe passed into tank body lower part, last step fermentor tank is provided with the discharge nozzle from tank body lower part pass-out, fermentor tank at different levels is provided with the air outlet from top pass-out, first step fermentor tank is also provided with the temperature increase penstock passed into tank base, described temperature increase penstock level runs through the bottom of first step fermentor tank to secondary fermentation tank, the temperature increase penstock at through position offers uniform tuyere upwards, last step fermentor tank also passes into the temperature increase water service pipe to tank body lower part.
For the benefit of discharge, the charging mouth of pipe of described discharge nozzle is lower than the discharging mouth of pipe of feed-pipe.
For weight reduction with prevent corrosion, described fermentor tank adopts plastic-steel tank to make.
For reaching high utilization rate, multistage fermentor tank adopts more than Pyatyi (comprising Pyatyi) fermentor tank.
Beneficial effect of the present invention:
The present invention's horizontal plastic-steel overlength tank for sewage gas adopts multistage natural pond method to prepare biogas, and clean environment firendly, utilization ratio high (improving the collection rate of 30%), saving resource, avoids waste.
Accompanying drawing illustrates:
Fig. 1 is the structural representation of one embodiment of the present invention.
Figure number identifies: 1, first step fermentor tank; 2, second stage fermentor tank; 3, third stage fermentor tank; 4, feed-pipe; 5, discharge nozzle; 6, temperature increase penstock; 6-1, tuyere; 7, air outlet; 8, temperature increase water service pipe; 9, port; 10, fourth stage fermentor tank; 11, level V fermentor tank; 12, the 6th grade of fermentor tank.
Embodiment:
Below in conjunction with accompanying drawing illustrated embodiment, technical scheme of the present invention is described further.
The main body of the present invention's horizontal plastic-steel overlength tank for sewage gas is six grades of fermentor tanks, is respectively the first step fermentor tank 1, second stage fermentor tank 2, third stage fermentor tank 3, fourth stage fermentor tank 10, level V fermentor tank 11 and the 6th grade of fermentor tank 12 that adopt plastic-steel to make.
First step fermentor tank 1, second stage fermentor tank 2, third stage fermentor tank 3, fourth stage fermentor tank 10, level V fermentor tank 11 and the 6th grade of fermentor tank 12 horizontal positioned from left to right, first step fermentor tank 1 is coaxially connected with second stage fermentor tank 2, second stage fermentor tank 2 is coaxially connected with third stage fermentor tank 3, third stage fermentor tank 3 is coaxially connected with fourth stage fermentor tank 10, fourth stage fermentor tank 10 is coaxially connected with level V fermentor tank 11, level V fermentor tank 11 is coaxially connected with the 6th grade of fermentor tank 12, port 9 by tank skin bottom between fermentor tank at different levels is communicated with, the top of fermentor tank at different levels is equipped with air outlet 7, as shown in Figure 1.
First step fermentor tank 1 is provided with feed-pipe 4 and temperature increase penstock 6, the discharging mouth of pipe of described feed-pipe 4 stretches to the bottom of tank body, described temperature increase penstock 6 (connection air pump) stretches to the bottom of tank body, and in first step fermentor tank 1 to second stage fermentor tank 2, third stage fermentor tank 3, fourth stage fermentor tank 10 and level V fermentor tank 11 bottom level extend, and the temperature increase penstock 6 of extending part offers uniform tuyere 6-1 upwards; 6th grade of fermentor tank 12 is provided with discharge nozzle 5 and temperature increase water service pipe 8, described discharge nozzle 5 stretches to the bottom of tank body, the charging mouth of pipe of discharge nozzle 5 is lower than the discharging mouth of pipe of feed-pipe 4, air pump supercharging can be utilized, waste residue, impurity waste material are discharged by discharge nozzle 5 at short notice, described temperature increase water service pipe 8 (connection water-heater) stretches to the bottom of tank body, solves the winter in some area, because temperature is too low and make the problem that natural pond function disappears, as shown in Figure 1.
Fermentation process of the present invention, its process is:
1, the air outlet 7 on fermentor tank at different levels is opened.
2, clear water is poured into by feed-pipe 4, the discharging mouth of pipe of the concordant feed-pipe 4 of clear water height.
3, close the air outlet 7 on fermentor tank at different levels, closing temperature adherence pressure pipe 6 and temperature increase water service pipe 8, open discharge nozzle 5.
4, the natural pond liquid of ight soil, sewage formation is by feed-pipe 4 charging, and accesses biogas bacterial classification.
5, in first step fermentor tank 1, carry out first step fermentation, then enter in second stage fermentor tank 2 and carry out second stage fermentation, then enter in third stage fermentor tank 3 and carry out third stage fermentation ... finally enter in the 6th grade of fermentor tank 12 and carry out the 6th grade of fermentation.
6, the biogas of fermentation comes together in tank body top, highly exceedes the natural pond liquid of tank body half, discharges under the effect of biogas pressure from discharge nozzle 5; For the natural pond liquid (waste residue mixed, impurity waste material and cause precipitation) being difficult to get rid of, need open temp adherence pressure pipe 6, by high-pressure jet rolling natural pond liquid, strengthen natural pond function, promote biogas temperature, increase biogas pressure, can rapidly natural pond liquid discharge nozzle 5 be discharged; Prepare biogas under low temperature, need open temp to promote water service pipe 8, to improve natural pond liquid temp, promote natural pond process.
Biogas is collected in the air outlet 7 of 7, opening on fermentor tank at different levels.
Claims (4)
1. horizontal plastic-steel overlength tank for sewage gas, comprise fermentor tank, it is characterized in that: described fermentor tank comprises multistage fermentor tank, in the horizontal direction, first step fermentor tank (1) is coaxially connected with second stage fermentor tank (2), second stage fermentor tank (2) is coaxially connected with third stage fermentor tank (3), by that analogy, be communicated with by the port (9) of tank skin bottom between fermentor tank at different levels, first step fermentor tank (1) is provided with the feed-pipe (4) passed into tank body lower part, last step fermentor tank is provided with the discharge nozzle (5) from tank body lower part pass-out, fermentor tank at different levels is provided with the air outlet (7) from top pass-out, first step fermentor tank (1) is also provided with the temperature increase penstock (6) passed into tank base, described temperature increase penstock (6) level runs through the bottom of first step fermentor tank (1) to secondary fermentation tank, the temperature increase penstock (6) at through position offers uniform tuyere (6-1) upwards, last step fermentor tank also passes into the temperature increase water service pipe (8) to tank body lower part.
2. horizontal plastic-steel overlength tank for sewage gas according to claim 1, is characterized in that: the charging mouth of pipe of described discharge nozzle (5) is lower than the discharging mouth of pipe of feed-pipe (4).
3. horizontal plastic-steel overlength tank for sewage gas according to claim 1, is characterized in that: described fermentor tank is plastic-steel tank.
4. according to the horizontal plastic-steel overlength tank for sewage gas in claims 1 to 3 described in any one, it is characterized in that: multistage fermentor tank is the above fermentor tank of Pyatyi.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610124010.5A CN105505751A (en) | 2016-03-04 | 2016-03-04 | Horizontal type plastic-steel super-long biogas tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610124010.5A CN105505751A (en) | 2016-03-04 | 2016-03-04 | Horizontal type plastic-steel super-long biogas tank |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105505751A true CN105505751A (en) | 2016-04-20 |
Family
ID=55714057
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610124010.5A Pending CN105505751A (en) | 2016-03-04 | 2016-03-04 | Horizontal type plastic-steel super-long biogas tank |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105505751A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107265812A (en) * | 2017-07-17 | 2017-10-20 | 钟康亮 | A kind of air pressure slag discharging environmental protection septic tank |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201245643Y (en) * | 2008-07-18 | 2009-05-27 | 马德顺 | Combined type methane generator |
CN101613658A (en) * | 2009-08-17 | 2009-12-30 | 吴兆流 | Biogas reaction device |
CN202359113U (en) * | 2011-11-08 | 2012-08-01 | 上海科文麦格里实业有限公司 | Large and medium multi-cavity combined biogas anaerobic fermentation device |
CN202744556U (en) * | 2012-08-15 | 2013-02-20 | 吉林省农业机械研究院 | Gas lifting double film covering garage bioreactor |
CN104710092A (en) * | 2015-04-08 | 2015-06-17 | 钟康亮 | Plastic steel biogas septic tank |
CN105296339A (en) * | 2015-12-04 | 2016-02-03 | 新蔡县青奎环保设备能源工程有限公司 | Power-free self-stirring automatic sludge discharge device for red mud biogas |
CN205420383U (en) * | 2016-03-04 | 2016-08-03 | 钟康亮 | Horizontal plastic steel overlength methane tank |
-
2016
- 2016-03-04 CN CN201610124010.5A patent/CN105505751A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201245643Y (en) * | 2008-07-18 | 2009-05-27 | 马德顺 | Combined type methane generator |
CN101613658A (en) * | 2009-08-17 | 2009-12-30 | 吴兆流 | Biogas reaction device |
CN202359113U (en) * | 2011-11-08 | 2012-08-01 | 上海科文麦格里实业有限公司 | Large and medium multi-cavity combined biogas anaerobic fermentation device |
CN202744556U (en) * | 2012-08-15 | 2013-02-20 | 吉林省农业机械研究院 | Gas lifting double film covering garage bioreactor |
CN104710092A (en) * | 2015-04-08 | 2015-06-17 | 钟康亮 | Plastic steel biogas septic tank |
CN105296339A (en) * | 2015-12-04 | 2016-02-03 | 新蔡县青奎环保设备能源工程有限公司 | Power-free self-stirring automatic sludge discharge device for red mud biogas |
CN205420383U (en) * | 2016-03-04 | 2016-08-03 | 钟康亮 | Horizontal plastic steel overlength methane tank |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107265812A (en) * | 2017-07-17 | 2017-10-20 | 钟康亮 | A kind of air pressure slag discharging environmental protection septic tank |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201148380Y (en) | Constant temperature highly effective biogas purification apparatus | |
CN106190788A (en) | The stirring of follow-on anaeroic digestor biogas slurry and broken shell circulation line | |
CN103923822B (en) | Stealthy multistage balance aerogenesis methane tank | |
CN102536602A (en) | Power generating device using sewage treatment plant tail water | |
CN105505751A (en) | Horizontal type plastic-steel super-long biogas tank | |
CN205382156U (en) | Handle rural organic marsh gas of rubbish pond | |
CN201746547U (en) | Dry fermentation biogas generation pit for rural household | |
CN201250233Y (en) | Tunnel biogas pool with water return on the top | |
CN204058453U (en) | Level Four pump around circuit methane-generating pit | |
CN206069667U (en) | Environmentally friendly feces, sewage purification bucket | |
CN205420383U (en) | Horizontal plastic steel overlength methane tank | |
CN203474794U (en) | Spiral type biogas fermentation tank capable of automatically discharging residues | |
CN205862244U (en) | Pulp-water device is taken out in a kind of wine brewing automatically | |
CN201296753Y (en) | Horizontal-flow biogas tank | |
CN201785384U (en) | Deflection tunnel type methane tank | |
CN205419917U (en) | Practical row of mud system | |
CN207375931U (en) | A kind of air pressure slag discharging environmental protection septic tank | |
CN201021452Y (en) | Methane pool for tunnel automatic extension in and out material | |
CN203602468U (en) | Round pool body composite six-stage anaerobic biogas digester | |
CN206089670U (en) | Feed liquid circulation fluidization fermenting installation | |
CN205188091U (en) | Large capacity marsh gas night -soil bucket | |
CN107265812A (en) | A kind of air pressure slag discharging environmental protection septic tank | |
CN201746545U (en) | Circulating methane generator | |
CN205011753U (en) | Utilize methane -generating pit of atmospheric pressure backward flow natural pond liquid | |
CN203999126U (en) | A kind of hydrolysis acidification pool |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160420 |