CN205367871U - Tertiary anaerobic fermentation device - Google Patents
Tertiary anaerobic fermentation device Download PDFInfo
- Publication number
- CN205367871U CN205367871U CN201521087245.9U CN201521087245U CN205367871U CN 205367871 U CN205367871 U CN 205367871U CN 201521087245 U CN201521087245 U CN 201521087245U CN 205367871 U CN205367871 U CN 205367871U
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- CN
- China
- Prior art keywords
- tower body
- liquid separator
- gas
- phase separator
- anaerobic
- 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
- 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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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model provides a tertiary anaerobic fermentation device, including tower body, water inlet, delivery port, three -phase separator, vapour and liquid separator, back flow and discharge, inside platform along the structure that is equipped with of tower body, divide into three -layer anaerobic reaction chamber with the tower body at the platform along last installation three -phase separator structure, the tower body in the bottom be equipped with the water inlet, the delivery port setting is at the top of tower body, the top of tower body still is equipped with vapour and liquid separator, vapour and liquid separator connection marsh gas pipe structure, vapour and liquid separator internally mounted's discharge is connected with three -layer anaerobic reaction chamber 's three -phase separator respectively, and vapour and liquid separator goes up, and the back flow that sets up is vertical to let in bottom in the tower body. The anaerobic fermentation speed of waste water can effectively be realized to whole device, and the reaction is more abundant, and manipulation processing is simple, can further popularize and apply to and the production and processing of industrialization.
Description
Technical field
This utility model relates to biogas facility field, is specifically related to a kind of three grades of anaerobic ferment devices.
Background technology
Biogas is as present clean energy resource, 21 century will be used widely, clean energy, and the pollution of environment is minimum, when waste water is continued to twist methane recovery, usually adopting the biological treatment of anaerobic reaction anaerobic waste water is environmental project and an important technology in energy project, is one of strong processing method of organic wastewater, is used for the process of the mud of municipal wastewater treatment plant, organic waste materials and part high concentrated organic wastewater thereof.
The anaerobic ferment devices design being usually used to now is relatively simple, and usually for pending sewage composition fermentation not exclusively, backflow and separation progression that anaerobic fermentation adopts are few, generally adopt one-level or secondary response, cause that reaction is insufficient, and gas production rate is relatively low.
Utility model content
For the deficiencies in the prior art, this utility model provides a kind of three grades of anaerobic ferment devices, it is possible to effectively realizes three grades of anaerobic reactions of device, improves anaerobic reaction speed.
For realizing object above, this utility model is achieved by the following technical programs:
A kind of three grades of anaerobic ferment devices, including tower body, water inlet, outlet, three phase separator, gas-liquid separator, return duct and discharge, described tower body interior is provided with platform along structure, three phase separator structure is installed on platform edge tower body is divided into three layers anaerobic reaction room, described tower body inner bottom part is provided with water inlet, outlet is arranged on the top of tower body, the top of described tower body is additionally provided with gas-liquid separator, gas-liquid separator connects biogas tubular construction, the internally installed discharge of described gas-liquid separator is connected with the three phase separator of three layers anaerobic reaction room respectively, and the return duct arranged on gas-liquid separator is vertically passed into tower body inner bottom part.
Preferably, described water inlet is provided with control valve.
Preferably, described platform is along being provided with sealing gland coil structures with three phase separator connecting portion.
Preferably, the height of described tower body is 10-15m.
Preferably, described three phase separator and platform are articulated and connected along structure.
This utility model provides a kind of three grades of anaerobic ferment devices, the platform arranged on device is along structure, tower body is divided into syllogic, and collect the biogas of generation respectively in gas-liquid separator by the discharge of the three phase separator on three sections, and refluxed in time by return duct, so that abundant reaction during anaerobic fermentation, the biogas of generation can be sent by gas-liquid separator in time that arrange on device by biogas pipe, and supply needs to utilize.Whole device is reasonable in design, simple to operate, can further genralrlization application.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, for those of ordinary skill in the art, under the premise not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 overall structure schematic diagram of the present utility model;
Wherein: 1, tower body;2, water inlet;3, outlet;4, three phase separator;5, return duct;6, discharge;7, gas-liquid separator;8, biogas pipe;101, platform edge.
Detailed description of the invention
For making the purpose of this utility model embodiment, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of this utility model protection.
nullAs shown in Figure 1,The present embodiment provides a kind of three grades of anaerobic ferment devices,Including tower body 1、Water inlet 2、Outlet 3、Three phase separator 4、Gas-liquid separator 7、Return duct 5 and discharge 6,Tower body 1 is internal is provided with platform along 101 structures,At platform, three phase separator 4 structure is installed along 101 and tower body 1 is divided into three layers anaerobic reaction room,The waste water that can realize passing into carries out multistage anaerobic reaction and processes,Improve efficiency of giving vent to anger,Tower body 1 inner bottom part is provided with water inlet 2,Outlet 3 is arranged on the top of tower body 1,The top of tower body 1 is additionally provided with gas-liquid separator 7,Gas-liquid separator 7 connects biogas pipe 8 structure,The internally installed discharge 6 of gas-liquid separator 7 is connected with the three phase separator 5 of three layers anaerobic reaction room respectively,And the return duct 5 arranged on gas-liquid separator 7 is vertically passed into tower body 1 inner bottom part,The gas component that can realize entering in gas-liquid separator 7 effectively refluxes.
Water inlet 2 is provided with control valve, can effectively control to enter the flow of waste water;Platform is provided with sealing gland coil structures along 101 with three phase separator 5 connecting portion, effectively prevents gas component from flowing out from the position, edge of contact;The height of tower body 1 is 10-15m, and separation efficiency now is best;Three phase separator 5 and platform are articulated and connected along 101 structures, can effectively realize disassembling function.
Above example only in order to the technical solution of the utility model to be described, is not intended to limit;Although this utility model being described in detail with reference to previous embodiment, it will be understood by those within the art that: the technical scheme described in foregoing embodiments still can be modified by it, or wherein portion of techniques feature is carried out equivalent replacement;And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of each embodiment technical scheme of this utility model.
Claims (4)
1. three grades of anaerobic ferment devices, including tower body, water inlet, outlet, three phase separator, gas-liquid separator, return duct and discharge, it is characterized in that, described tower body interior is provided with platform along structure, three phase separator structure is installed on platform edge tower body is divided into three layers anaerobic reaction room, described tower body inner bottom part is provided with water inlet, outlet is arranged on the top of tower body, the top of described tower body is additionally provided with gas-liquid separator, gas-liquid separator connects biogas tubular construction, the internally installed discharge of described gas-liquid separator is connected with the three phase separator of three layers anaerobic reaction room respectively, and the return duct arranged on gas-liquid separator is vertically passed into tower body inner bottom part, described three phase separator and platform are articulated and connected along structure.
2. three grades of anaerobic ferment devices as claimed in claim 1, it is characterised in that described water inlet is provided with control valve.
3. three grades of anaerobic ferment devices as claimed in claim 1, it is characterised in that described platform is along being provided with sealing gland coil structures with three phase separator connecting portion.
4. three grades of anaerobic ferment devices as claimed in claim 1, it is characterised in that the height of described tower body is 10-15m.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201521087245.9U CN205367871U (en) | 2015-12-23 | 2015-12-23 | Tertiary anaerobic fermentation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201521087245.9U CN205367871U (en) | 2015-12-23 | 2015-12-23 | Tertiary anaerobic fermentation device |
Publications (1)
Publication Number | Publication Date |
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CN205367871U true CN205367871U (en) | 2016-07-06 |
Family
ID=56259966
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201521087245.9U Expired - Fee Related CN205367871U (en) | 2015-12-23 | 2015-12-23 | Tertiary anaerobic fermentation device |
Country Status (1)
Country | Link |
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CN (1) | CN205367871U (en) |
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2015
- 2015-12-23 CN CN201521087245.9U patent/CN205367871U/en not_active Expired - Fee Related
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160706 Termination date: 20161223 |