CN201962286U - Barm liquid processing system - Google Patents
Barm liquid processing system Download PDFInfo
- Publication number
- CN201962286U CN201962286U CN2010206323367U CN201020632336U CN201962286U CN 201962286 U CN201962286 U CN 201962286U CN 2010206323367 U CN2010206323367 U CN 2010206323367U CN 201020632336 U CN201020632336 U CN 201020632336U CN 201962286 U CN201962286 U CN 201962286U
- Authority
- CN
- China
- Prior art keywords
- barm
- efficient cyclone
- pipeline
- barm liquid
- air
- 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
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model patent discloses a barm liquid processing system, which comprises a primary high-efficient separator, a secondary high-efficient separator, a centrifugal fan, a barm liquid outlet pipeline, and a clean air return pipeline, wherein under the action of the negative pressure of the centrifugal fan, barm liquid reaches the primary high-efficient separator through the barm liquid outlet pipeline, most of barm breaks in the primary high-efficient separator and is resolved into fermentation broth and air, the fermentation broth flows back into a fermentation tank through a post-separation return pipeline under the action of gravity, and the air and a small amount of the barm liquid enter the secondary high-efficient separator; and the barm liquid breaks and is separated, the generated fermentation broth joins the post-separation return pipeline through the barm liquid outlet pipeline and flows back into the fermentation tank, and the generated air returns into the fermentation tank through the centrifugal fan and the clean air return pipeline.
Description
Affiliated technical field
The utility model relates to a kind of device of handling the foam solution that produces in the fermenting process, when relating in particular to maximum and utilizing fermentor tank volumetrical situation.
Background technology
Aerobic fermentation is an aerobic fermentation, needs a large amount of sterile airs, to satisfy the metabolism of aerophil, obtains tunning.Particularly along with the expansion of fermentative production scale and the employing of novel process, the unit volume ferment strength of fermentor tank is increased, the uncontaminated air demand enlarges rapidly in the fermenting process, air compressor machine wind collecting port air input and fermentor tank free air delivery also increase thereupon, and the amount of air circulation in the production space increases.Because of having drop and foam to be taken out of in the fermentation exhaust, cause viable bacteria bulk diffusion, be easy to generate phage, contain rich nutrient substances in the foam solution simultaneously, cause a large amount of breedings of assorted bacterium easily, the assorted bacterium amount in fermentative production space is increased, Air quality descends, increase the air filtering system burden, influence is produced.
Summary of the invention
Problem to be solved in the utility model provides a kind of barm liquid treating system, with the foam solution that produces in the fermenting process in time, dispose efficiently, avoids a large amount of breedings of assorted bacterium in the fermentative production space and the generation of phage.
For addressing the above problem, the technical solution adopted in the utility model is: add a cover barm liquid treating system at the fermentor tank top, this system comprise foam solution outlet conduit, efficient cyclone, secondary efficient cyclone, centrifugal blower, a clean wind answer back pipeline, separate the back back liquid pipeline, be characterized under the effect of centrifugal blower negative pressure, barm liquid arrives an efficient cyclone through the foam solution outlet conduit, carry out break apart, generate fermented liquid and air, fermented liquid under action of gravity, the back liquid pipeline fermentor tank that refluxes back after separating; Air and uncracked foam enter the secondary efficient cyclone, carry out break apart, the fermented liquid of generation by pipeline with separate the back back liquid pipeline and converge, the fermentor tank that refluxes back, the air of generation is got back to fermentor tank once more through centrifugal blower, the clean wind pipeline of answering back.
The beneficial effects of the utility model are: the foam that produces in the fermenting process is in time by break apart, avoided the substratum nutritive substance to be taken out of, thereby a large amount of breedings of assorted bacterium and the generation of phage have been avoided, and make and put tank volume and improve 5% one 15%, the defoamer consumption reduces 50%-90%, has reduced production cost.
Description of drawings
Below in conjunction with drawings and Examples the utility model will be further described explanation.
Among the figure: 1. efficient cyclone, 2. secondary efficient cyclone, 3. centrifugal blower, 4. foam solution outlet conduit, 5. clean wind pipeline of answering back, 6. separate back back liquid pipeline, 7. fermentor tank venting port, 8. barm liquid layer
Embodiment
With reference to accompanying drawing, this barm liquid treating system comprises an efficient cyclone (1), secondary efficient cyclone (2), centrifugal blower (3), foam solution outlet conduit (4), the clean wind pipeline (5) of answering back, separate back back liquid pipeline (6), when barm liquid layer (8) touches foam solution outlet conduit (4), under the effect of centrifugal blower (3) negative pressure, barm liquid arrives an efficient cyclone (1) through foam solution outlet conduit (4), carry out break apart, generate fermented liquid and air, fermented liquid back liquid pipeline (6) after separating fermentor tank that refluxes back, air and uncracked foam solution enter secondary efficient cyclone (2), carry out break apart, the fermented liquid back liquid pipeline (6) after separating that produces, be back to fermentor tank, the air that produces after the lather collapse is through centrifugal blower (3), the clean wind pipeline (5) of answering back is got back to fermentor tank once more.
Claims (3)
1. barm liquid treating system, comprise efficient cyclone, secondary efficient cyclone, centrifugal blower, foam solution outlet conduit, clean wind pipeline of answering back, it is characterized in that: under the centrifugal blower suction function, the foam solution that produces in the fermenting process enters efficient cyclone and even secondary efficient cyclone, carry out break apart, the fermented liquid that produces after the break apart is back in the fermentor tank under action of gravity, and clean gas is in centrifugal blower is transferred back fermentor tank.
2. barm liquid treating system according to claim 1 is characterized in that: the level attitude of secondary efficient cyclone is higher than the position of an efficient cyclone.
3. barm liquid treating system according to claim 1 is characterized in that: the level attitude of foam solution outlet conduit is lower than the level attitude of fermentor tank venting port, and the answer back level attitude of pipeline of clean wind is higher than the level attitude of foam solution outlet conduit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206323367U CN201962286U (en) | 2010-11-24 | 2010-11-24 | Barm liquid processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206323367U CN201962286U (en) | 2010-11-24 | 2010-11-24 | Barm liquid processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201962286U true CN201962286U (en) | 2011-09-07 |
Family
ID=44524820
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206323367U Expired - Fee Related CN201962286U (en) | 2010-11-24 | 2010-11-24 | Barm liquid processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201962286U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635741A (en) * | 2016-12-01 | 2017-05-10 | 沈奇光 | Fermentation tank overflow collecting, separating and recycling device |
| CN111718829A (en) * | 2020-06-23 | 2020-09-29 | 佛山市海天（江苏）调味食品有限公司 | Method for treating liquid vinegar fermentation foam |
| CN111849737A (en) * | 2020-06-10 | 2020-10-30 | 北京首钢朗泽新能源科技有限公司 | Fermentation system and method |
| CN117299724A (en) * | 2023-11-29 | 2023-12-29 | 龙焱能源科技（杭州）有限公司 | Glass cleaning and bubble removing device |
-
2010
- 2010-11-24 CN CN2010206323367U patent/CN201962286U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635741A (en) * | 2016-12-01 | 2017-05-10 | 沈奇光 | Fermentation tank overflow collecting, separating and recycling device |
| CN111849737A (en) * | 2020-06-10 | 2020-10-30 | 北京首钢朗泽新能源科技有限公司 | Fermentation system and method |
| CN111849737B (en) * | 2020-06-10 | 2021-05-04 | 北京首钢朗泽新能源科技有限公司 | Fermentation system and method |
| CN111718829A (en) * | 2020-06-23 | 2020-09-29 | 佛山市海天（江苏）调味食品有限公司 | Method for treating liquid vinegar fermentation foam |
| CN117299724A (en) * | 2023-11-29 | 2023-12-29 | 龙焱能源科技（杭州）有限公司 | Glass cleaning and bubble removing device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Arora et al. | Bioreactors in solid state fermentation technology: Design, applications and engineering aspects | |
| CN201962286U (en) | Barm liquid processing system | |
| CN101698817B (en) | Method for producing white wine by distilled grain continuous solid state fermentation | |
| CN101538532B (en) | External loop air lift type membrane bioreactor | |
| CN103103128A (en) | Method for high efficiency enrichment culture of microalgae | |
| CN105543314A (en) | Method for producing polymyxin E through fermentation and foam separation coupling | |
| CN111334407A (en) | Process technology and process equipment for preparing yeast culture by deep fermentation of yeast | |
| WO2008156299A3 (en) | Air circulating system of fermentation chamber | |
| CN101845407A (en) | Actinobacillus and method for producing succinic acid | |
| CN206198875U (en) | The device of waste gas after a kind of fermentation for treatment | |
| CN103962365A (en) | Kitchen waste treatment process with reclamation, harmlessness and reduction | |
| CN202819562U (en) | Feed fermentation sealing barrel with one-way valve | |
| CN201520758U (en) | Foam return fermentation system | |
| CN102492614A (en) | Microbial fermentation method for solid and liquid phase separation | |
| CN206014887U (en) | A kind of fermentation tank for being provided with deep layer air intake installation | |
| CN101822168A (en) | Methods for inoculating edible fungus strain and culturing mycelium and device thereof | |
| CN204111735U (en) | A kind of fermentation system with thalli separation facility | |
| CN108570430A (en) | A kind of lactobacillus delbruockii subspecies bulgaricus and preparation method thereof | |
| CN202509078U (en) | Lactic acid fermentation device based on dual-bacterium fermentation | |
| CN202936410U (en) | Gas-liquid separation device for itaconic acid exhaust | |
| CN207468624U (en) | A kind of microorganism fermentation tank gas circulation device | |
| CN201709370U (en) | Feedstuff fermentation sealing bag with one-way valve | |
| CN202011872U (en) | Recovery device of fermentation liquor spilled from fermentation tank for citric acid production | |
| CN201665641U (en) | Device for extracting and collecting fermented alcohol | |
| CN202778111U (en) | Separating device of riboflavin fermenting tail gas |
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 |
Granted publication date: 20110907 Termination date: 20181124 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |