CN201206146Y - Anaerobic fermentation apparatus based on adsorbent biological desorption and regeneration principle - Google Patents
Anaerobic fermentation apparatus based on adsorbent biological desorption and regeneration principle Download PDFInfo
- Publication number
- CN201206146Y CN201206146Y CN 200820055205 CN200820055205U CN201206146Y CN 201206146 Y CN201206146 Y CN 201206146Y CN 200820055205 CN200820055205 CN 200820055205 CN 200820055205 U CN200820055205 U CN 200820055205U CN 201206146 Y CN201206146 Y CN 201206146Y
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- chamber
- valve
- arm
- absorbent
- utility
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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
- C12M23/58—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
- 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
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- Bioinformatics & Cheminformatics (AREA)
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- Biotechnology (AREA)
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- General Health & Medical Sciences (AREA)
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- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
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- Oil, Petroleum & Natural Gas (AREA)
- Treatment Of Sludge (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to anaerobic fermentation technical field, which adopts absorbent to transfer fatty acid in an acidification phase container to a methane phase container and produces methane according to the absorbent biological desorption regeneration theory. The utility model solves the technical problems of the prior methane preparation device such as big size, large water consumption, inconvenience for loading and transportation of reaction material, low gas production speed, inconvenience for controlling the gas production amount, and the like. The utility model is characterized in that the absorbent is installed in reaction cavities through inner surface structure of a sealing port; a sealing cover conducts sealing through outer surface structure of the sealing port; the intervals of all the cavities are connected with a breathing master pipe through breathing branch pipes arranged at the upper parts of the cavities; connecting branch pipes at the lower parts of the cavities are connected with a connecting master pipe and connected to a adjusting cavity through the connecting master pipe; and valves are arranged on all pipes. The utility model enables feed liquid to contact with the absorbent and adjusts the contacting area of the feed liquid and the absorbent through the effects of the valves in the pipeline and the adjusting cavity, thereby further adjusting the gas production amount and air pressure, and the adjusting cavity can heat the feed liquid which enters the adjusting cavity.
Description
Technical field
The utility model relates to the technical field of anaerobically fermenting, particularly relates to a kind of technology that anaerobically fermenting is produced biogas that is used for.
Background technology
The utility model is according to two-phase anaerobically fermenting and adsorbing agent biological desorption and regeneration principle, utilize the carrier of sorbent material as fermentation back lipid acid, lipid acid in the acidifying phase container is transferred to methane phase container, utilize adsorbing agent biological desorption and regeneration principle, in the process that generates methane, finish the biological desorption and regeneration of sorbent material.Technical problems the such as at present device for preparing biogas by anaerobically fermenting exists volume big, and water consumption is many, and reaction material is difficult for loading transportation, and aerogenesis is slow, gas production rate is wayward.
The content of utility model
At the defective that exists in the above-mentioned prior art, technical problem to be solved in the utility model provides that a kind of volume is little, water saving, aerogenesis are fast, gas production rate is easy to control, reaction material is easy to transportation and the reaction material carrier can be through regeneration and reusable anaerobic ferment devices.
In order to solve above-mentioned technical problem, a kind of anaerobic ferment devices provided by the utility model is the multi-cavity body structure, comprise an adjusting chamber that has piston, at least one reaction chamber, sealing cover, sorbent material, the common air chamber, the ventilation arm, the ventpipe valve, be communicated with house steward, be communicated with arm, communicating pipe valve, it is characterized in that: sorbent material is installed in the reaction chamber by the seal inner surface structure, sealing cover seals by the seal outer surface structure, link to each other with the common air chamber by its top ventilation arm between each reaction chamber, ventilation arm and common air chamber are provided with valve, being communicated with arm by its underpart between each reaction chamber communicates with the connection house steward, and communicate with regulating the chamber by being communicated with house steward, the connection arm be communicated with house steward and be provided with valve.Further, described anaerobic ferment devices is characterized in that: described anaerobic ferment devices is provided with regulates the chamber, and described adjusting chamber is at least one or more the combination in the following structure:
1) piston;
2) piston chamber;
3) heating subsystem.
Further, described anaerobic ferment devices is characterized in that: the heating subsystem is at least one or more the combination in the following structure:
1) regulates the bottom, chamber and be provided with electric heating panel;
2) wall in adjusting chamber scribbles heat absorbing coating;
3) piston face scribbles heat absorbing coating.
Description of drawings
This accompanying drawing is the structural representation of utility model embodiment.
Embodiment
Below in conjunction with description of drawings the utility model embodiment is described in further detail, but present embodiment is not limited to the utility model, every employing analog structure of the present utility model and similar variation thereof all should be listed protection domain of the present utility model in.
As shown in drawings, a kind of anaerobic ferment devices provided by the utility model is the multi-cavity body structure, comprise an adjusting chamber that has piston 7, piston chamber 8, electric heating panel 12 and heat absorbing coating 13 to constitute, at least one reaction chamber 1, sealing cover 3, sorbent material 2, common air chamber 4, ventilation arm 5, ventpipe valve 6, be communicated with house steward 9, be communicated with arm 10, communicating pipe valve 11.
Concrete using method is as follows:
1) when reaction chamber all as the dress liquid situation of methane phase container
Before feed liquid is injected reaction chamber, the reaction chamber that the sorbent material 2 that is adsorbed with lipid acid is put into and fix after, cover 3, the second steps of sealing cover, open the valve 6 of the arm 5 of respectively ventilating, close the valve 11 that is communicated with house steward 9, in reaction chamber 1, inject the liquid material, contact when liquid level is increased to sorbent material 2 by the feed liquid input terminus, biological desorption begins, methane just can generate, and dress is after liquid finishes, and closes communicating pipe valve 11.
2) when the dress liquid situation of reaction chamber part as acidifying phase container
According to needing, before feed liquid is injected reaction chamber 1, need open as ventilation arm 5 valves 6 of the reaction chamber 1 of acidifying phase container, connected component tube valve 11 as the reaction chamber 1 of acidifying phase container is closed, and this reaction chamber 1 promptly can be used as acidifying phase container, meanwhile, all the other are closed as the valve 6 of the ventilation arm 5 of the reaction chamber 1 of non-acidizing phase container, common air chamber 4 valve 6 is closed, and is communicated with house steward 9 and closes towards the valve 11 of piston chamber 8, and these reaction chambers 1 are as methane phase container.Under above-mentioned state, import acidizing fluid from the feed liquid input terminus toward container, after input finishes, close the valve 6 of ventilation arm 5 of the reaction chamber 1 of acidifying phase container, open the valve 6 of ventilation arm 5 of the reaction chamber 1 of methane phase container then, carry out the feed liquid input of methane phase container, use step) with situation 1, open the valve 6 of ventilation arm 5 of the reaction chamber 1 of acidifying phase container then, close the sealing cover 3 of acidifying phase container.
3) adjusting of gas generating amount and air pressure
3.1) adjusting by force of gas generating amount and air pressure:
Open the valve 11 and the valve 11 that is communicated with house steward 9 of the connection arm 10 of selected reaction chamber 1, the valve 11 of the connection arm 10 in remaining reaction chamber 1 is closed, suction function by piston 7, bacterium liquid in the selected reaction chamber 1 is transferred to piston chamber 8 by force, close the valve 11 of the connection arm 10 of this reaction chamber 1 then.Bacterium liquid enters into piston chamber 8, and liquid level descends in the selected reaction chamber 1, reduces with the sorbent material contact surface, and the tolerance growing amount reduces thereupon, and air pressure amplification is slowed down, and the atmosphere storage space in this reaction chamber 1 increases simultaneously, and air pressure reduces.Need increase gas production rate again, only need bacterium hydraulic pressure in the piston chamber 8 is returned former reaction chamber 1, and close the valve 11 of the connection arm 10 of this reaction chamber 1, stop bacterium liquid to be back to former reaction chamber 1 and get final product.
3.2) other approach
Guaranteeing under the safe situation, also can directly directly inject bacterium liquid or acidizing fluid, regulating gas production rate and air pressure by direct adding or minimizing sorbent material by seal.
4) heating
Can also can under the situation that meteorological conditions allows, absorb sunlight by heat absorbing coating the liquid material is heated by the electric heating panel energising of regulating the bottom, chamber is heated.
This device also can be used for the occasion of other anaerobically fermentings, is not limited only to the production of methane.
Claims (3)
1, a kind of device that is used for anaerobically fermenting, this device is the multi-cavity body structure, comprise and regulate the chamber, at least one reaction chamber, sealing cover, sorbent material, the common air chamber, the ventilation arm, the ventpipe valve, be communicated with house steward, be communicated with arm, communicating pipe part such as valve, it is characterized in that: sorbent material is installed in the reaction chamber by the seal inner surface structure with its coupling, sealing cover seals by the seal outer surface structure with its coupling, link to each other with the common air chamber by its top ventilation arm between each reaction chamber, ventilation arm and common air chamber are provided with valve, being communicated with arm by its underpart between each reaction chamber communicates with the connection house steward, and communicate with regulating the chamber by being communicated with house steward, the connection arm be communicated with house steward and be provided with valve.
2, according to the described device that is used for anaerobically fermenting of claim 1, it is characterized in that: described anaerobic ferment devices is provided with regulates the chamber, and described adjusting chamber is at least one or more the combination in the following structure:
1) piston;
2) piston chamber;
3) heating subsystem.
3, according to the described device that is used for anaerobically fermenting of claim 2, it is characterized in that: the heating subsystem is at least one or more the combination in the following structure:
1) regulates the bottom, chamber and be provided with electric heating panel;
2) wall in adjusting chamber scribbles heat absorbing coating;
3) piston face scribbles heat absorbing coating.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200820055205 CN201206146Y (en) | 2008-01-29 | 2008-01-29 | Anaerobic fermentation apparatus based on adsorbent biological desorption and regeneration principle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200820055205 CN201206146Y (en) | 2008-01-29 | 2008-01-29 | Anaerobic fermentation apparatus based on adsorbent biological desorption and regeneration principle |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201206146Y true CN201206146Y (en) | 2009-03-11 |
Family
ID=40465213
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 200820055205 Expired - Fee Related CN201206146Y (en) | 2008-01-29 | 2008-01-29 | Anaerobic fermentation apparatus based on adsorbent biological desorption and regeneration principle |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201206146Y (en) |
-
2008
- 2008-01-29 CN CN 200820055205 patent/CN201206146Y/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 | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090311 Termination date: 20120129 |