CN2457164Y - Energy saving fermentation tank - Google Patents
Energy saving fermentation tank Download PDFInfo
- Publication number
- CN2457164Y CN2457164Y CN 00267163 CN00267163U CN2457164Y CN 2457164 Y CN2457164 Y CN 2457164Y CN 00267163 CN00267163 CN 00267163 CN 00267163 U CN00267163 U CN 00267163U CN 2457164 Y CN2457164 Y CN 2457164Y
- Authority
- CN
- China
- Prior art keywords
- fermentor tank
- jet mixer
- air
- conservation
- energy
- 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
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
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
-
- 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/14—Pressurized fluid
Landscapes
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Zoology (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model relates to an energy saving fermentation tank. The basic structure comprises a tank body, a mechanical stirring device and multistage jet mixing devices, wherein the multistage jet mixing device comprises an air distributor which is arranged on the bottom of the tank body and is connected with a compressed air inlet pipe. The air distributor is uniformly distributed with three to eight air nozzles, and a two stage or a multistage jet mixing device is arranged along the jet direction on the back of each nozzle. The fermentation tank is also provided with circular air intake pipes which are uniformly distributed and are communicated with the corresponding jet mixing devices, the air above the liquid face is drawn to the bottom of the fermentation tank, and the best dissolved oxygen effect is achieved by the least air consumption.
Description
The utility model relates to a kind of energy-conservation fermentor tank, belongs to technical field of chemical, is particularly useful for aerobic fermentation.
In biotechnology, the fermenting process of aerobic microorganism mostly is to adopt to feed the pressurized air bubbling and mechanical stirring is set to realize oxygen supply.And the fermentor tank that widely adopts generally all adopts single port air inlet or the air inlet of annular spread pipe, cooperates with lower floor's paddle and smashes bubble, increases the gas-to-liquid contact area, realizes gas-liquid mass transfer.This type of fermentor tank dissolved oxygen effect is general, and the electric energy that air compressor and mixer drive consumed is bigger.Be that generally to be used for churned mechanically installed power be 2-2.4kw/m to example with the penicillin fermentation
3Fermented liquid is about 1-1.3m and feed compressed air require
3/ m
3The fermented liquid per minute is amounted to air compressor machine power and is roughly 3.5-4.6kw/m
3Fermented liquid stirs and ventilation power consumption sum is 5.5-7kw/m
3Fermented liquid accounts for the total cost significant proportion.So how to reduce power consumption, reduce running cost is the fermentation important topic that the insider studied always.The U.S. once adopted six flat-blade turbines to strengthen power of agitator to 3.5kw/m
3Fermented liquid, the air consumption is reduced to 0.3-0.5m simultaneously
3/ m
3The fermented liquid per minute is obtained same ferment effect, though total power has descended, has brought the increase of fermentor tank thermal load simultaneously, does not obtain promoting.Chinese patent 97236557 has related to a kind of High oxygen solubility ferment pot, utilize compressed-air actuated kinetic energy, adopt aerating apparatus commonly used in the environmental protection as gas liquid mixer, receive respectively in some branches of air line, improve dissolved oxygen by the turbulence of gas-liquid in mixing tank, each mixer outlet can be along the peripheral jet of same circumference to substitute lower floor's stirring rake, under the situation that does not improve the mechanical stirring power consumption simultaneously, reduce the air consumption, can play certain effect.Its shortcoming is as not removing lower floor's paddle, air input reduces and will cause churned mechanically power consumption to rise, and after lower floor's stirring is removed, it mixes and smashes the bubble defunctionalization, and can rise rapidly because of buoyancy from the micro-bubble of the oxygen enrichment fermented liquid of mixing tank ejection, so leaning against in the process by jet mixer substantially entirely, the fermented liquid dissolved oxygen of fermentor tank bottom obtains.And, just determined that the gas-liquid mass transfer of fermented liquid of fermentor tank bottom is low than middle and upper part efficient because of the limitation of air inlet amount and jet mixer quantity, and inhomogeneous, actual test proves that also the fermentor tank top and the bottom dissolved oxygen situation of this kind structure differs bigger.Above-mentioned in addition High oxygen solubility ferment pot all is that pressurized air passes the fermentation liquid layer after pot bottom enters the same with general fermentor tank for utilizing on the mode of air, is discharged by vapor pipe from the air that the fermented liquid liquid level is overflowed.Because of the solubleness of oxygen in water very little, pressurized air rises at the bottom of the jar the process more than the fermentation liquid level has only minimum part of oxygen to be utilized, with the penicillin fermentation is example, fermenting after testing, oxygen content has only 1% of air capacity to be utilized in the above air of liquid level, rise to the above residual air of liquid level and still have utility value, recycling then can reduce the consumption of fresh air by the utilization ratio that improves oxygen in the air at the bottom of it if can being caused jar.
The purpose of this utility model is to solve the low and uneven situation of fermentor tank bottom gas-liquid mass transfer efficient; Effectively utilize the compressed-air actuated problem in liquid level top.
The utility model is achieved by the following scheme: this energy-conservation fermentor tank, basic structure comprises tank body, mechanical stirring device and multistage jet flow mixing device, multistage jet flow mixing device comprises that tank base is provided with the air-distributor that links to each other with compressed air inlet pipe, uniform 3-8 air nozzle on sparger, behind each nozzle, all the one-level jet mixer is installed, coaxial installation secondary jets mixing tank or multistage jet mixer behind the one-level jet mixer along its injection direction.
Described energy-conservation fermentor tank is provided with uniform circulation air suction pipe and communicates with corresponding jet mixer, the air suction pipe fermentor tank liquid level top that is arranged at suitable for reading.
The catchment port of the secondary jets mixing tank of described energy-conservation fermentor tank can link to each other with the outlet of one-level jet mixer and constitute closed induction chamber, and induction chamber is connected with air suction pipe.
The catchment port of the secondary jets mixing tank of described energy-conservation fermentor tank does not link to each other with the outlet of one-level jet mixer, the uncovered fermented liquid that directly places.
Install hybrid element additional in the diffusive mixing chamber of the last step jet mixer of described energy-conservation fermentor tank.
The axis of every group of jet mixer of described energy-conservation fermentor tank and horizontal direction angle are the 0-35 degree.
The axis of every group of jet mixer of described energy-conservation fermentor tank in the horizontal direction projection and this projection plane on the jet mixer angle that is exported to jar center radius be the 0-90 degree.
The multistage jet flow mixing device of described energy-conservation fermentor tank can be installed one or more layers in fermentor tank.
The utility model has the advantages that from the above air of liquid level is recycled and increase fermented liquid strengthen jar by the cycle index of mixing tank in two angles of tank body bottom dissolved oxygen of fermentation liquid especially, be implemented in the best dissolved oxygen effect of acquisition under the minimum air consumption.
Further specify embodiment of the present utility model (is example with the secondary jets mixing tank) below in conjunction with accompanying drawing:
Fig. 1 thinks hybrid element synoptic diagram Fig. 5 and is the uncovered multistage jet mixer synoptic diagram figure that places among the fermentor tank liquid for the Kenny is installed in the secondary jets mixing tank for multistage jet mixer structural representation Fig. 4 of Fig. 2 for multistage jet mixer vertical view Fig. 3 of Fig. 1 for air circulating type fermentor tank diagrammatic cross-section Fig. 2: 1, stirrer 2, fermentation tank body 3, air suction pipe 4, agitating vane 5, air-distributor 5-1, air nozzle 6, jet mixer 6-1, one-level jet mixer 6-2, secondary jets mixing tank 6-3, induction chamber 6-4, the Kenny thinks hybrid element 7, support 8, inlet pipe 9, vapor pipe
Provide the air-breathing fermentor tank of a kind of circulation among Fig. 1, comprise tank body 2, mechanical stirring device 1,4, secondary jets mixing tank 6, wherein connect air-distributor 5 at compressed air inlet pipe 8 ends, uniform 3-8 tapering is the taper air nozzle 5-1 of 7-15 degree on it, 30-80mm installs first step jet mixer 6-1 along its injection direction behind each air nozzle, its front end is flaring catchment port, the rear end is pre-large post-small, axial section is hyp diffusive mixing chamber, the coaxial installation of 30-80mm second stage jet mixer 6-2 behind first step jet mixer 6-1, its front end is flaring catchment port, and the rear end is pre-small post-large, axial section is hyp diffusive mixing chamber.Jet mixers at different levels all are fixed on the tank body by support 7.
Mode according to Fig. 1: the catchment port of second stage jet mixer 6-2 links to each other with the outlet of first step jet mixer 6-1, it is isolated to constitute airtight induction chamber 6-3 and fermented liquid, air suction pipe 3 one ends link to each other with induction chamber 6-3, and an end links to each other with the air that ferments more than the liquid level.Under this kind fit system, first step jet mixer 6-1 is as the gas-liquid jet mixer, aspirate fermented liquid by airstream by air nozzle 5-1 ejection, make gas-liquid carry out efficient mass transfer in the indoor violent turbulence of diffusive mixing, secondary jets mixing tank 6-2 is as the liquid-gas jet mixing tank, aspirate air more than the fermentation liquid level by the oxygen enrichment fermented liquid jet that is sprayed by one-level jet mixer 6-1, reenter the recycle that realizes air in the fermented liquid environment after in secondary jets mixing tank 6-2, carrying out gas-liquid mass transfer once more at the bottom of making it to get back to once more jar.Utilization ratio by oxygen in this kind mode air can improve more than 1 times, and then can reduce the amount of fresh air that feeds in fermentor tank in a large number, and can obtain good dissolved oxygen effect.
Fig. 5: the another kind of mode that is used that provides the front and back stages jet mixer, the catchment port of secondary jets mixing tank 6-2 is uncovered to be arranged in the fermented liquid, in this way, one-level jet mixer 6-1 aspirates fermented liquid as the gas-liquid jet mixer by the airstream by air nozzle 5-1 ejection equally, in the diffusive mixing chamber of one-level jet mixer 6-1, form the oxygen enrichment fermented liquid, and two jet mixer 6-2 are as the liquid liquid mixer, the oxygen enrichment fermented liquid jet that is sprayed by one-level jet mixer 6-1 aspirates on every side oxygen deprivation fermented liquid reinforcing mass transfer once more in the diffusive mixing chamber, when having utilized compressed-air actuated kinetic energy more fully, also can improve fermented liquid obtains gas-liquid mass transfer at every turn by jet mixer internal circulating load greatly like this, increase the cycle index of fermented liquid by jet mixer, can significantly improve in the fermentor tank the especially mass-transfer efficiency of middle and lower part fermented liquid and homogeneity, to improve whole dissolved oxygen level.
In addition, be further enhancing mixed effect, the duration of contact of prolongation gas-liquid is all kinds of hybrid elements of the indoor installation of diffusive mixing of one-level jet mixer in the end, and 6-4 thinks hybrid element for the Kenny among Fig. 4.
Aforementioned multi-staged air jet mixing system generally is installed on fermentor tank bottom center place, also can in jar one or more layers be installed according to actual needs.
The churned mechanically lower floor stirring arm of fermentor tank can remove, air-distributor 5 links to each other with air intake duct 8, middle position at the bottom of placing jar, the pyramid type air nozzle 3 of uniform 4 bendings on it, the injection direction of each nozzle in the horizontal direction projection and this projection plane on jet mixer to be exported to a jar center radius angle be 45 degree, and turn to consistent with stirring.Along its injection direction one-level jet mixer 6-1 is installed at distance air jet 50mm place, the coaxial installation secondary jets of 50mm mixing tank 6-2 behind the one-level jet mixer, the outlet place circle diameter of 4 secondary jets mixing tanks be tank body diameter about 1/3rd.The axis of each mixing tank and horizontal direction angle are 15 degree.The catchment port of secondary jets mixing tank 6-2 links to each other with the outlet of one-level jet mixer 6-1, constitutes airtight induction chamber 6-3, isolates with fermented liquid, and air suction pipe 3 one ends are connected with induction chamber 6-3, and the other end is opened on the above space of fermentation liquid level in the fermentor tank.
Claims (8)
1. energy-conservation fermentor tank, basic structure comprises tank body (2), mechanical stirring device (1,4) and multistage jet flow mixing device (6), it is characterized in that multistage jet flow mixing device comprises that tank base is provided with the air-distributor (5) that links to each other with compressed air inlet pipe (8), uniform 3-8 air nozzle (5-1) on sparger, behind each nozzle, all one-level jet mixer (6-1) is installed, coaxial installation secondary jets mixing tank (6-2) or multistage jet mixer behind the one-level jet mixer along its injection direction.
2, energy-conservation fermentor tank according to claim 1 is characterized in that fermentor tank is provided with uniform circulation air suction pipe (3) and communicates with corresponding jet mixer (6), the air suction pipe fermentor tank liquid level top that is arranged at suitable for reading.
3, energy-conservation fermentor tank according to claim 2, the catchment port that it is characterized in that secondary jets mixing tank (6-2) link to each other with the outlet of one-level jet mixer (6-1) and constitute closed induction chamber (6-3), and induction chamber is connected with air suction pipe (3).
4, energy-conservation fermentor tank according to claim 1 is characterized in that the catchment port of secondary jets mixing tank (6-2) does not link to each other the uncovered fermented liquid that directly places with the outlet of one-level jet mixer (6-1).
5, energy-conservation fermentor tank according to claim 1 is characterized in that installing hybrid element (6-4) additional in the diffusive mixing chamber of last step jet mixer.
6, energy-conservation fermentor tank according to claim 1 is characterized in that the axis of every group of jet mixer and horizontal direction angle are the 0-35 degree.
7, energy-conservation fermentor tank according to claim 1, the axis that it is characterized in that every group of jet mixer in the horizontal direction projection and this projection plane on the jet mixer angle that is exported to jar center radius be the 0-90 degree.
8, energy-conservation fermentor tank according to claim 1 is characterized in that multistage jet mixes device and can in fermentor tank one or more layers be installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00267163 CN2457164Y (en) | 2000-12-14 | 2000-12-14 | Energy saving fermentation tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00267163 CN2457164Y (en) | 2000-12-14 | 2000-12-14 | Energy saving fermentation tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2457164Y true CN2457164Y (en) | 2001-10-31 |
Family
ID=33621064
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00267163 Expired - Fee Related CN2457164Y (en) | 2000-12-14 | 2000-12-14 | Energy saving fermentation tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2457164Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100358996C (en) * | 2006-02-14 | 2008-01-02 | 南通圣诺鑫生物科技有限公司 | Semi-gas-lifting type jet aeration fermentation energy-saving device |
| CN102443536A (en) * | 2010-10-09 | 2012-05-09 | 新奥科技发展有限公司 | Auxiliary device for photobioreactor |
| CN105925464A (en) * | 2016-07-12 | 2016-09-07 | 王继丰 | Air ejector with own power rotation arranged at bottom of biological fermentation tank |
| CN112744887A (en) * | 2019-10-29 | 2021-05-04 | 中国石油化工股份有限公司 | Jet flow air floating device |
-
2000
- 2000-12-14 CN CN 00267163 patent/CN2457164Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100358996C (en) * | 2006-02-14 | 2008-01-02 | 南通圣诺鑫生物科技有限公司 | Semi-gas-lifting type jet aeration fermentation energy-saving device |
| CN102443536A (en) * | 2010-10-09 | 2012-05-09 | 新奥科技发展有限公司 | Auxiliary device for photobioreactor |
| CN102443536B (en) * | 2010-10-09 | 2014-07-30 | 新奥科技发展有限公司 | Auxiliary device for photobioreactor |
| CN105925464A (en) * | 2016-07-12 | 2016-09-07 | 王继丰 | Air ejector with own power rotation arranged at bottom of biological fermentation tank |
| CN105925464B (en) * | 2016-07-12 | 2018-05-18 | 王继丰 | A kind of air ejector mounted on biofermentation pot bottom with rotation of relying on oneself |
| CN112744887A (en) * | 2019-10-29 | 2021-05-04 | 中国石油化工股份有限公司 | Jet flow air floating device |
| CN112744887B (en) * | 2019-10-29 | 2022-07-12 | 中国石油化工股份有限公司 | Jet flow air floating device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1326783C (en) | Aerator and advanced waste water treatment method using the same | |
| CN102732417B (en) | Emulsifying-type aerobic fermentation tank | |
| CN212451400U (en) | Compound microbial fermentation jar convenient to wash | |
| CN2457164Y (en) | Energy saving fermentation tank | |
| CN100358996C (en) | Semi-gas-lifting type jet aeration fermentation energy-saving device | |
| CN2334762Y (en) | High oxygen solubility ferment pot | |
| CN201376917Y (en) | Solid liquid flow mixing device of anaerobic reactor | |
| CN2727166Y (en) | Swirl mixed strong cyclic aerator | |
| CN102634443A (en) | Abnormal fermenting device for microalgae | |
| CN101285034B (en) | Multifunctional and composite type foam-preventing recovery device for biofermentation | |
| CN2890062Y (en) | Cyclone and inflation combined biochemical reactor | |
| CN101508486A (en) | Anaerobic reactor tridimensional flow agitating apparatus | |
| CN2272782Y (en) | Jet multistage gas-liquid mixing apparatus | |
| CN209685762U (en) | Stir fermentation system | |
| CN2204803Y (en) | Dual circulating aerating lifting fertilizing tank with mixing components | |
| CN112791629B (en) | Vertical double-curve stirring impeller and stirrer thereof | |
| CN2201173Y (en) | Gas-liquid mixer of bioreactor | |
| CN2550372Y (en) | Double circulation gas stirring anaerobic fermentation tank | |
| CN2142464Y (en) | High oxygen solubility injection mixer | |
| CN208395175U (en) | Outer tube bubble retention formula fermentor | |
| CN202465363U (en) | Low pressure oxygenation jet apparatus | |
| CN202164295U (en) | Circular spray-type aerobic fermentation device | |
| CN2736362Y (en) | Semi-air-lift device for double spray ring of fermenter | |
| CN2573501Y (en) | Wind stirring fermentation tank | |
| CN2205388Y (en) | Fermentation tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |