CN201206145Y - Methane balanced pressure gathering apparatus for anaerobic reactor - Google Patents
Methane balanced pressure gathering apparatus for anaerobic reactor Download PDFInfo
- Publication number
- CN201206145Y CN201206145Y CNU2008200333404U CN200820033340U CN201206145Y CN 201206145 Y CN201206145 Y CN 201206145Y CN U2008200333404 U CNU2008200333404 U CN U2008200333404U CN 200820033340 U CN200820033340 U CN 200820033340U CN 201206145 Y CN201206145 Y CN 201206145Y
- Authority
- CN
- China
- Prior art keywords
- biogas
- tank body
- anaerobic reactor
- weighing apparatus
- methane
- 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 - Lifetime
Links
Images
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
- C12M23/40—Manifolds; Distribution pieces
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/40—Means for regulation, monitoring, measurement or control, e.g. flow regulation of pressure
-
- 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)
- Zoology (AREA)
- Organic Chemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Genetics & Genomics (AREA)
- General Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Biochemistry (AREA)
- Microbiology (AREA)
- General Health & Medical Sciences (AREA)
- Biotechnology (AREA)
- Biomedical Technology (AREA)
- Clinical Laboratory Science (AREA)
- Molecular Biology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to a methane steady pressure collecting device used for an anaerobic reactor, which comprises a methane steady pressure tank and a methane collecting pipeline of a triphase separator connecting the methane steady pressure tank and the anaerobic reactor. The methane steady pressure tank comprises multistage front-back arranged tank bodies, and the multistage tank bodies are connected in series and form multistage hydroseals. The pressure of the gas cavity of the previous stage tank body increases by the hydroseal effect of the next stage tank body. The stage treatment of the methane steady pressure tank saves the production cost, and is convenient for device arrangement, and enhances stability and maneuverability of the device.
Description
Technical field
The utility model relates to a kind of biogas weighing apparatus that is used for anaerobic reactor and presses collection device.
Background technology
In field of waste water treatment, the anaerobic treatment technology is development in recent years one of direction faster.Particularly for the processing of highly difficult trade effluents such as high concentrated organic wastewater, the anaerobic treatment technology has become main flow wastewater processing technology both domestic and external.But relatively the present situation and the foreign level of the exploitation of China's anaerobic treatment process also have gap, say on the slave unit that the coordinative composition of equipments of China is relatively poor, how to make standardization, standardization and simplification be still problem demanding prompt solution.
Anaerobic reactor can produce biogas, generally carries out three phase separation by the separator in the reactor.Make separator reach good separating effect, just need effective biogas weighing apparatus to press collection device to cooperate with it.The structure that at present traditional biogas weighing apparatus is pressed jar is anticipated as shown in Figure 1, generally comprises: the collecting methane pipeline that separator and biogas weighing apparatus in the anaerobic reactor pressed jar is pressed jar, connected to the biogas weighing apparatus.Traditional biogas weighing apparatus is pressed and jar is adopted an one-level water seal, is positioned at situation below the anaerobic reactor liquid level for the separator liquid level, needs very high water seal height, and the tank body height can be very big, is unfavorable for saving cost, has shortcomings such as poor stability, operation inconvenience simultaneously.Produce foam or scum silica frost through regular meeting in the separator of anaerobic reactor, influence the normal conveying of three phase separation effect and biogas.Traditional collecting methane pipeline does not consider how to tackle, and brings big inconvenience to operation when going wrong.
The utility model content
The utility model purpose is that the biogas weighing apparatus that provides a kind of simple in structure, cost economic, operation to be used for anaerobic reactor easily in order to overcome the deficiencies in the prior art is pressed collection device.
For achieving the above object, the technical solution adopted in the utility model is: a kind of biogas weighing apparatus that is used for anaerobic reactor is pressed collection device, comprise that biogas weighing apparatus presses jar, connects described biogas weighing apparatus and press jar collecting methane pipeline with the triphase separator of anaerobic reactor, described biogas weighing apparatus presses jar to be made up of the tank body that multistage front and back are provided with, and described multistage tank body is in series and is connected to form multilevel water seal, by the water seal effect of level tank body afterwards the air chamber pressure in the prime tank body is improved.
Further, a plurality of inlet pipe that described collecting methane pipeline comprises the effuser that is connected with the triphase separator of anaerobic reactor, is connected and is connected with described effuser, the degree of depth that the end of described a plurality of inlet pipe gos deep in the one-level tank body has nothing in common with each other, the multilayer inlet pipe is set in the tank body simultaneously, inlet pipe stretches into water seal height and regulates according to the pressure needs in the anaerobic reactor, the air pressure of the fixed different sizes that can weigh simultaneously.
Described collection tube comprises gas collection standpipe and gas collection transverse tube, and described gas collection standpipe adopts four-way to be connected with the gas collection transverse tube, and the end of gas collection standpipe and gas collection transverse tube adopts the blind flange end socket, carries out clear and coherent thereby can dismantle easily to effuser and separator inside.
Because the utilization of technique scheme, the utility model compared with prior art has following advantage: owing to press the tank body of jar to carry out stage treatment the biogas weighing apparatus, not only saved cost, be convenient to the layout of equipment simultaneously, strengthened stabilization of equipment performance and operability.
Description of drawings
Accompanying drawing 1 is the structural representation that traditional biogas weighing apparatus is pressed jar;
Accompanying drawing 2 is pressed the structural representation of collection device for the utility model biogas weighing apparatus;
Accompanying drawing 3 is pressed the structural representation of jar for the utility model biogas weighing apparatus;
Accompanying drawing 4 is the utility model collecting methane piping node structure enlarged diagram;
Accompanying drawing 5 is traditional collecting methane piping node structure enlarged diagram;
Wherein: 10, the biogas weighing apparatus is pressed jar; 1, tank body; 2, inlet pipe; 3, inlet pipe; 4, communicating pipe; 8, tank body; 13, gas collection standpipe; 14, gas collection transverse tube; 17, blind flange; 18, blind flange;
20, collecting methane pipeline;
30, effuser;
Embodiment
Below in conjunction with accompanying drawing, describe particular content of the present utility model in detail for example:
The biogas weighing apparatus that is used for the anaerobic waste water reactor is as shown in Figure 2 pressed collection device, and it comprises biogas weighing apparatus pressure jar 10, collecting methane pipeline 20.Described biogas weighing apparatus presses jar 10 to form by being in series before and after the multistage tank body to be provided with, and presses a jar classification setting by weighing, and can reach the fixed effect than the large level biogas pressure that weighs with less water seal tank body.
Press the structure and the principle thereof of jar to describe in detail below in conjunction with Fig. 3 to the biogas weighing apparatus:
Biogas weighing apparatus shown in Figure 3 presses jar 10 to replace original big tank body by volume less one-level tank body 1 and secondary tank body 8, one-level tank body 1 is in series by communicating pipe 4 with secondary tank body 8 and is connected, and the end of communicating pipe 4 stretches in the secondary tank body 8, according to pressure principle, communicating pipe 4 ends A, the pressure of B is identical, when the end of communicating pipe 4 stretches in the secondary tank body 8 that contains certain depth of water, then this moment is by the water seal effect of this secondary tank body 8, the air chamber pressure of one-level tank body 1 is improved, thereby avoid using the bigger tank body of volume to realize a biogas weighing apparatus pressure jar interior higher gaseous tension, therefore saved manufacturing cost greatly.Usually be arranged in anaerobic reactor top eminence owing to this equipment simultaneously, the stability that reduces to help equipment of height, operator have also made things convenient for many to the control of valve, water level etc.
Other structure divisions of one-level tank body 1 and secondary tank body 8 still can adopt the structural pattern of traditional tank body, has the water-in that is connected with the water supply installation (not shown) as each tank body, tank body is provided with liquidometer, can regulate moisture storage capacity in the tank body by valve.Simultaneously, secondary tank body top also offers the air outlet, and this air outlet is connected with follow-up biogas treatment unit (not shown), is used to biogas treatment unit conveying biogas, and said structure is not the utility model structural feature, does not repeat them here.
Collecting methane pipeline 20 comprise the effuser 30 that is connected with the triphase separator of anaerobic reactor, be connected with effuser 30 stretch to inlet pipe 2,3 in the one-level tank body 1, the water seal height that inlet pipe 2,3 stretches in the tank body 1 has nothing in common with each other, therefore, can regulate various inlet pipe 2,3 according to the pressure needs in the anaerobic reactor and stretch into the degree of depth of water seal, thus the air pressure of the fixed different sizes that can weigh simultaneously.In the utility model, stretch into inlet pipe in the one-level tank body 1 and be not limited in the present embodiment two, many inlet pipe can be set according to the actual needs.
Effuser 30 adopts the four-way mode of connection to be formed by connecting by gas collection standpipe 13 and gas collection transverse tube 14 usually; as shown in Figure 4; because the separator in the anaerobic reactor produces foam or scum silica frost through regular meeting; adopt traditional threeway effuser as shown in Figure 5 can not well solve foam or scum problem; thereby influence the effect of three phase separation and the normal conveying of biogas; by adopting the mode of connection of four-way; and the end at each body adopts blind flange 17 to block; can be convenient to dismounting effuser and triphase separator inside are carried out clear and coherent, thereby can effectively avoid the problems referred to above.
Claims (4)
1, a kind of biogas weighing apparatus that is used for anaerobic reactor is pressed collection device, comprise that biogas weighing apparatus presses jar (10), connects described biogas weighing apparatus and press jar collecting methane pipeline (20) with the triphase separator of anaerobic reactor, it is characterized in that: described biogas weighing apparatus presses jar (10) to be made up of the tank body (1,8) that multistage front and back are provided with, and described multistage tank body (1,8) is in series and is connected to form multilevel water seal, by the water seal effect of level tank body (8) afterwards the air chamber pressure in the prime tank body (1) is improved.
2, the biogas weighing apparatus that is used for anaerobic reactor according to claim 1 is pressed collection device, it is characterized in that: described collecting methane pipeline (20) comprise the effuser (30) that is connected with the triphase separator of anaerobic reactor, with a plurality of inlet pipe (2,3) that described effuser (30) is connected and is connected, the degree of depth that the end of described a plurality of inlet pipe (2,3) gos deep in the one-level tank body (1) has nothing in common with each other.
3, the biogas weighing apparatus that is used for anaerobic reactor according to claim 2 is pressed collection device, it is characterized in that: described effuser (30) comprises gas collection standpipe (13) and gas collection transverse tube (14), and described gas collection standpipe (13) adopts four-way to be connected with gas collection transverse tube (14).
4, the biogas weighing apparatus that is used for anaerobic reactor according to claim 3 is pressed collection device, and it is characterized in that: the end of described gas collection standpipe (13) and gas collection transverse tube (14) removably is connected with blind flange (17,18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200333404U CN201206145Y (en) | 2008-03-19 | 2008-03-19 | Methane balanced pressure gathering apparatus for anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200333404U CN201206145Y (en) | 2008-03-19 | 2008-03-19 | Methane balanced pressure gathering apparatus for anaerobic reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201206145Y true CN201206145Y (en) | 2009-03-11 |
Family
ID=40465212
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200333404U Expired - Lifetime CN201206145Y (en) | 2008-03-19 | 2008-03-19 | Methane balanced pressure gathering apparatus for anaerobic reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201206145Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103266052A (en) * | 2013-05-22 | 2013-08-28 | 尹四兴 | Self-adaptive type biogas generating and collecting system |
| CN109942085A (en) * | 2019-03-20 | 2019-06-28 | 上海交通大学 | A kind of continuous flow up-flow aerobic granular sludge reactor |
-
2008
- 2008-03-19 CN CNU2008200333404U patent/CN201206145Y/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103266052A (en) * | 2013-05-22 | 2013-08-28 | 尹四兴 | Self-adaptive type biogas generating and collecting system |
| CN109942085A (en) * | 2019-03-20 | 2019-06-28 | 上海交通大学 | A kind of continuous flow up-flow aerobic granular sludge reactor |
| CN109942085B (en) * | 2019-03-20 | 2021-10-08 | 上海交通大学 | Continuous flow upflow type aerobic granular sludge reactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204474409U (en) | Rectilinear anaerobic aerobic integratedization reactor | |
| CN201206145Y (en) | Methane balanced pressure gathering apparatus for anaerobic reactor | |
| CN204237619U (en) | A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor | |
| CN209493371U (en) | A kind of integral type large size MBR film group device | |
| CN204224316U (en) | Novel anaerobic reactor | |
| CN204356140U (en) | A kind of anaerobic biological reactor | |
| CN204874046U (en) | High rigidity water softens system's device | |
| CN202063751U (en) | Wastewater recycling device for water purifier | |
| CN103114484A (en) | Recovery and comprehensive utilization method of waste heat of rotary spherical digester | |
| CN202532443U (en) | Novel steam condensate water recycling device | |
| CN206121466U (en) | Multistage membrane separation natural pond gas purification device | |
| CN204298093U (en) | A kind of high-efficiency dissolued-air pipe | |
| CN205204908U (en) | Anaerobism, good oxygen series connection biochemical treatment test device | |
| CN212894139U (en) | Novel oxygen-free water preparation equipment | |
| CN102995709A (en) | Household wastewater classification collection and classification reutilization device | |
| CN208980414U (en) | Interior circulation is folded to upflow type anaerobic biological treatment device | |
| CN204079596U (en) | High concentrated organic wastewater two phase anaerobic integrated treatment unit | |
| CN202403254U (en) | Low-pressure steam utilizing system | |
| CN202594856U (en) | Internal recycling reactor capable of being adjusted and reinforced | |
| CN206838703U (en) | A kind of high-efficient cleaning system | |
| CN206635178U (en) | A kind of construction site Waster water reuse apparatus | |
| CN202346869U (en) | Sewage treatment device | |
| CN201506996U (en) | Water storage pressurizing system and horizontal pressure type water tank used in system | |
| CN201424388Y (en) | Urea process wastewater recovering device | |
| CN204469667U (en) | A kind of vacuum system for the production of silicone sealant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: JIANGSU SUZHOU PURIFICATION ENVIRONMENTAL ENGINEER |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 215122 ZHONGXIN TECHNOLOGY CITY, NORTH OF LOUZHONG ROAD, SUZHOU CITY INDUSTRIAL PARK, JIANGSU PROVINCE TO: 215122 ZHONGXIN TECHNOLOGY CITY,NO.2, WEIXIN ROAD, INDUSTRIAL PARK, SUZHOU CITY,JIANGSU PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20100331 Address after: 215122 new science and Technology City, No. 2, Xin Lu, Suzhou Industrial Park, Jiangsu, China Patentee after: Jiangsu Sujing Group Co., Ltd. Patentee after: Suzhou Sujing Enviromental Technology Co., Ltd. Address before: 215122 north central new science and Technology City, middle Lou Road, Suzhou Industrial Park, Jiangsu Patentee before: Jiangsu Sujing Group Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20090311 |
|
| CX01 | Expiry of patent term |