CN101020887A - Fruit vinegar fermenting tank - Google Patents
Fruit vinegar fermenting tank Download PDFInfo
- Publication number
- CN101020887A CN101020887A CN 200610105161 CN200610105161A CN101020887A CN 101020887 A CN101020887 A CN 101020887A CN 200610105161 CN200610105161 CN 200610105161 CN 200610105161 A CN200610105161 A CN 200610105161A CN 101020887 A CN101020887 A CN 101020887A
- Authority
- CN
- China
- Prior art keywords
- tank body
- tank
- fruit vinegar
- air
- inlet
- 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.)
- Granted
Links
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The fruit vinegar fermenting tank includes a sandwiched tank body with a blow down port in the bottom, a material inlet port, an air exhaust port and an observation window; a coiler and a temperature controlling probe inside the tank; a centrifugal pump; a spraying system connected to the centrifugal pump; an air intake system comprising an air intake pipe, an air filter and an air flow rate regulator; and a discharge/sampling port. The fruit vinegar fermenting tank has the centrifugal pump for circulating the liquid and well combined air intake system and spraying system to complete air-liquid mixing and oxygen transfer. It has simple structure, easy sterilizing, great oxygen dissolving amount, high acetic acid producing efficiency, low cost and other features, and may be used for liquid acetic acid fermentation and other aerobic fermentation engineering.
Description
Technical field
The invention belongs to the biotechnology apparatus field, relate to a kind of liquid deep layer aerobic fermentation bio-reactor, particularly a kind of novel fruit vinegar fermentor tank.
Background technology
The development of biology source is the new discovery of biotechnology the principles of science, and it has directive function to the application field.Principle will instruct production practice, is used for producing, must be by this important bridge of bio-reactor.So-called bio-reactor (Bioreactor) also claims fermentor tank in microbial fermentation, being meant to provide controllable environment, to satisfy cell normal growth and biosynthetic device.Its position of in various biological processings, plying in the centre.Although bio-reactor relates to the process of producing some biological product with animal body or plant materials, modal bio-reactor is the device that biological respinse is achieved, just biotechnology specific equipment---fermentor tank.
Because the biotechnology research extensively and profoundly and the continuous development of biological industry, so far existing multiple bio-reactor is applied to produce, and wherein major biotechnology special purpose reactor has: mechanical agitation type fermentor tank, bubbling fermentation tank, airlift fermentor, membrane bioreactor, self-suction fermentor, solid substances fermentor tank etc. are several.The acetic fermentation jar that is applied to fruit vinegar production mainly contains bubbling fermentation tank, airlift fermentor, self-suction fermentor and automatic sprinkling type fermentor tank.The principle of work of bubbling fermentation tank is to utilize the bubble that feeds in the substratum to drive liquid and produce mixing when rising, and the oxygen in the bubble used for the thalline in the substratum, it is simple in structure, easy handling, running cost is low, mixes and the mass-and heat-transfer better performances, and no drive disk assembly in the reactor, sealing easily is to keeping aseptic condition favourable.Airlift fermentor is to grow up on the basis of bubbling fermentation tank, and it is to utilize the ejection function of air and fluid severe difference to cause reaction solution to circulate, and realizes stirring, mixing and the transmission oxygen of liquid, macroscopical good mixing effect in the reactor; Simple in structure, movement-less part, easy cleaning is difficult for microbiological contamination; Heat and mass efficient height can solve the mass transfer mixed problem of fermentation systems such as high-density, high viscosity, high pol preferably; Fluidization is effective, can make solid particulate keep suspended state fully; Waste of energy is even, and the shearing force sensitive materials is had special meaning.The major parts of self-suction fermentor is the hollow turbine agitator of prism, when it rotates in container, impel liquid to flow fierce turbulence, agitator paddle kinetic energy is on every side increased and the potential energy minimizing, form vacuum to a certain degree, suck ambient atmos by the conduit that connects with the hollow turbine of agitator, realize gas-to-liquid contact and mix mass transfer.The automatic sprinkling type fermentor tank is a most frequently used fermentor tank in the present vinegar production, it is to utilize impeller pump to make the zymophyte bed that the fermented liquid circulated sprinkling makes with stopping composition such as corn cob, reed rods and the fermentor tank that carries out acetic fermentation, it is simple in structure, the production efficiency height, good product quality, but the loaded down with trivial details and easy pollution microbes of bacterium bed treatment process, a large amount of generations because of the vinegar film especially often make production be forced to interrupt.
Fruit vinegar and fermented drink thereof contain rich organic acid, amino acid, VITAMIN etc., have Ginseng Extract, refresh oneself, effect such as production of sperm quenches the thirst, improve a poor appetite, fat-reducing, reducing blood-fat, be good seasonings and protective foods, at home, the world market all is in great demand very much.As cider vinegar, grape vinegar, SHANGSHENCU, persimmon vinegar, apricot vinegar etc., the look delicious food is good, doting on of occidentals extremely, and domestic demand also is ascendant trend rapidly.Along with the development of modern medicine and Food science, people more and more pay attention to the health protection effect of diet, and fruit vinegar is exactly a kind of novel vinegar that grows up for this needs that satisfy people.It adopts fruit, melon and fruit is main raw material, brewages through acetic fermentation to form.Contain more natural aromatic material and non-volatility organic acid in the fruit, like this, compare with normally used vinegar, vinegar by the fruit brew has kept the distinctive fruital of fruit, tart flavour is gentleer to be closed, and nutrition such as rich vitamin, trace element, many kinds all have certain nourishing function, thereby have improved its edibleness and economic worth.In addition, through the fruit vinegar of different processing treatment, can be used as beverage after the diluted allotment and directly drink.Because these advantages of fruit vinegar, so fruit vinegar just has been subjected to consumers in general's warm welcome once coming out, become hotel, restaurant, dining room, huge numbers of families, everybody drinks, every household daily life consumer's goods of usefulness all, has huge market potential and vast potential for future development.Developing of fruit vinegar industry must be with its crucial production unit---and the research and development of acetic fermentation jar are prerequisite, and fruit vinegar production is badly in need of having the acetic fermentation jar appearance that facility investment is low, easy and simple to handle, efficient is high, energy consumption is low, pollutions is little, can adapt to different industrial scale needs.
A good bio-reactor should satisfy following requirement:
1. vertebration, stand the sterilization repeatedly of steam, inner wall smooth, corrosion resistance and good is beneficial to sterilize thoroughly and reduces the influence of metal ion to biological respinse;
2. good gas-liquid-solid contact and mixed performance and heat, quality, momentum transfer performance are efficiently arranged;
3. under the prerequisite that keeps biological respinse to require, cut down the consumption of energy;
4. good thermal exchange performance is arranged, to keep the biological respinse optimum temperuture;
5. the control of feasible pipeline ratio and instrument arranged, be applicable to disinfecting action and automatization control.
If the advantage of the comprehensive bubbling style of energy, air lift type and self-suction fermentor, and overcome effectively automatic sprinkling type fermentor tank bacterium bed handle loaded down with trivial details, easily produce drawback such as vinegar film, develop more simple in structure, be easy to sterilizing and washing, dissolved oxygen amount big, produce sour efficient height, easy handling, applied widely, that cost is low, that satisfy above-mentioned requirements, acetic fermentation jar with independent intellectual property right, to promoting China's vinegar (especially fruit vinegar) and other aerobic fermentation industrial expansions of bioengineering field, have great importance.
Summary of the invention
The objective of the invention is to, a kind of novel fruit vinegar fermentor tank is provided.This fruit vinegar fermentor tank utilizes fluid mechanics principle, adopt novel inlet system, can reach that air flow is big, dissolved oxygen is fast, gas-liquid mixed is even, be suitable for disinfecting action and automatization control, and structure is more simple, easy handling, efficient height, energy consumption is low, safety performance good, applied widely, cheap.
The technical scheme that realizes the foregoing invention purpose is: a kind of fruit vinegar fermentor tank, comprise tank body, it is characterized in that, described tank body is an interlayer, in establish serpentine tube, tank base is provided with sewage draining exit, the side-lower of tank body is equipped with impeller pump, impeller pump is connected with injection system, inlet system and discharge port/thief hole, and this inlet system comprises inlet pipe, air filter and air regulator; The tank body top is provided with opening for feed, venting port and viewing window.
Also be provided with temperature probe in tank body and the interlayer, this temperature probe is communicated with control panel.Above-mentioned tank body top also has mechanical defoaming device, and mechanical defoaming device is communicated with venting port, and the foam probe that is communicated with mechanical defoaming device is housed in the venting port.Liquidometer and control panel are equipped with in the side of tank body.
Fruit vinegar fermentor tank of the present invention is power with the impeller pump, by the unique design of inlet system and the conversion of injection system, form the overall circulation in order of gas-liquid-solid mixture, have simple in structure, be easy to sterilizing and washing, dissolved oxygen amount big, produce sour efficient height, easy handling, applied widely, running cost is low, lower-price characteristic.Use this fermentor tank and can save equipment such as air compressor in the air-purification system, water cooler, water-and-oil separator, air accumulator, total filter, also can reduce area of mill site, overall estimation approximately can reduce facility investment 30-50%.This fermentor tank can also be widely used in all many-sides of bioengineering field aerobic fermentation except that applying to the liquid acetic acid fermentation, have broad application prospects.
Description of drawings
Fig. 1 is a general plane structural representation of the present invention;
Fig. 2 is inlet system of the present invention and airway essential structure figure;
Fig. 3 is the air intake system structure schema of several increase air flows.
The present invention is described in further detail below in conjunction with accompanying drawing.
Embodiment
Referring to Fig. 1, Fig. 1 is a specific embodiment of the present invention, its constitutional features comprises tank body 1, this tank body 1 is an interlayer, tank body 1 bottom is provided with sewage draining exit 10, the side-lower of tank body 1 is equipped with impeller pump 2, and impeller pump 2 is connected with injection system 4, inlet system 3 and discharge gate (or being called thief hole) 9, and this inlet system 3 comprises inlet pipe, air filter and air regulator; Tank body 1 top is provided with opening for feed 7, venting port 8, viewing window 12 and mechanical defoaming device 6; Mechanical defoaming device 6 is communicated with venting port 8, and the foam probe 13 that is communicated with mechanical defoaming device 6 is housed in the venting port 8, and liquidometer 11 and control panel 5 also are equipped with in the side of tank body 1.
Tank body 1 is stainless steel or special plastic sandwich design, in establish serpentine tube and temperature probe, show by the temperature variation in the temperature probe monitor fermentation jar and on control panel 5, when temperature in the jar surpasses setting range, chimes of doom be can send, steam valve or cold valves adjustment temperature opened to remind the staff; The power of impeller pump 2 and lift, inlet system 3 can be according to the throughput apolegamys of fermentor tank with the unitized construction of injection system 4; The inlet pipe of inlet system 3 is connected with digital display airflow measuring device, and shows and the adjusting air flow quantity by control panel 5; Mechanical defoaming device 6 is connected with venting port 8, the foam monitoring probe 13 that is communicated with mechanical defoaming device 6 is installed in the venting port 8, when because of the big submergence foam monitoring of foam volume probe 13, mechanical defoaming device 6 is promptly started working, and is carrying secretly foam enters high speed rotating from the gas-liquid import the rotary drum or rotor (1000r/min-1450r/min) when air draft, and foam is broken rapidly, and by means of action of centrifugal force, make liquid and air separation, clean wind is discharged from exhaust duct, and fermented liquid is in return line returns jar.
The airway structure of inlet system is referring to accompanying drawing 2, the contriver discovers: according to fluid mechanics principle, on impeller pump and rising pipe that tank body is connected, promptly at the vertical insertion in the 10cm～20cm place of distance mouth spray 102 airway 101, airway 101 insertion ends are 30 ° of angles, angle faces water (flow) direction, and the caliber ratio of rising pipe and airway 101 is no more than 1: 0.5 and is advisable.
The structure of the inlet system 3 of increase air flow is referring to accompanying drawing 3, wherein the mouth spray 102 of figure (a) is the single hose structure, the mouth spray 102 of figure (b) is a T shape tubular construction, the mouth spray 102 of figure (c) is for there being a plurality of liquid mouths above the T shape pipe, the mouth spray 102 of figure (d) is a single tube, a plurality of liquid mouths are arranged above, and the mouth spray 102 of figure (e) is a single tube, and the different liquid mouth of a plurality of length is arranged above.The contriver is through discovering: under impeller pump power and lift certain condition, the orientation that unitized construction and injection system by conversion inlet system 3 and injection system 4 is connected with tank body 1 (as changing the angle that sprays the mouth of pipe and jar inwall, reduce the spray tube caliber, adjusting the position of spray tube mouth of pipe place tank body etc.), can increase air flow, with the requirement of the fermentor tank that satisfies different throughput to air flow.
The effect of injection system 4 is to realize the fierce turbulence of fermented liquid by adjusting the injection direction of shower nozzle in jar, thereby obtains maximum volumetric oxygen transfer coefficient.
Injection system 4 is one tunnel air inlet multichannel shower nozzles, or multichannel air inlet multichannel shower nozzle, and its best injection direction is that the inwall of shower nozzle and tank body 1 is tangential direction, and small canister can adopt one tunnel air inlet multichannel shower nozzle and tank body 1 inwall in vertical direction.
On the fruit vinegar fermentor tank basis of the foregoing description, after removing the temperature probe and control panel 5, mechanical defoaming device 6 and additional facilities such as foam monitoring probe 13 and liquidometer 11 in the tank body interlayer, additional simpler and easy cooling and lagging facility on tank body 1, easy fruit vinegar fermentor tank can be made, small-sized production-scale needs can be directly satisfied.The specific embodiment that the contriver provides is, adopt the plastics circular tank, remove temperature controlling system and control panel 5, machinery bubble device 6 and additional facilities such as foam monitoring probe 13 and liquidometer 11 disappear, design 300 liters of simple and easy fermentor tanks, it is 450W that this simple and easy fermentor tank adopts the power of impeller pump, lift is 8M, carry out the test of persimmon vinegar acetic fermentation through twice in Shaanxi Province's Tongchuan City Yintai District 99 red vinegars industry company limited, the result shows: at the kind vinegar 150L of inoculation acidity 5.4g/100ml, add the fresh persimmon distiller's wort 150L of edible ethanol 4.5L and alcoholic strength 6% (v/v), keep fermented liquid acidity being reached more than the 5.0g/100ml in 24 hours under the situation of air flow 260L/min.
Novel fruit vinegar fermentation tank of the present invention by the improvement of air intake system structure, is compared with existing technology the present invention, brings following obvious technique effect:
1. gas handling system 3 makes liquid force Rapid Circulation, at outlet pipe under the effect of centrifugal pump 2 Vertical junction with wireway forms certain vacuum, makes ambient atmos by the wireway suction and with the spray of liquid stream Inject in the tank, make the circulation of liquid stream suck air and fierce turbulence takes place in tank, realize gas-liquid contact and mixed Close mass transfer, no any transmission device in the tank body namely without mechanical agitation, relies on centrifugal pump to make liquid fully Circulate, and realize that by gas handling system and the ingenious combination of spraying system gas-liquid is mixed and the biography of oxygen Pass.
2. realize the structural design of maximal ventilatory volume: the method for attachment by adjusting the mouth of a river and tank body, Pipe diameter size or the version of conversion air inlet spraying system can adapt to the ventilation of different capabilities fermentation tank The amount requirement.
3. the whole moulding design of tank body: by temperature regulation and control system, throughput regulation and control system, The configuration of air cleaning system etc. realizes semi-automatic or full-automatic controlled fermentation.
Claims (6)
1. fruit vinegar fermentor tank, comprise tank body (1), it is characterized in that, described tank body (1) is an interlayer, be provided with serpentine tube in the interlayer, tank body (1) bottom is provided with sewage draining exit (10), and the side-lower of tank body (1) is equipped with impeller pump (2), impeller pump (2) is connected with injection system (4), inlet system (3) and discharge port/thief hole (9), and this inlet system (3) comprises inlet pipe, air filter and air regulator; Tank body (1) top is provided with opening for feed (7), venting port (8) and viewing window (12).
2. fruit vinegar fermentor tank as claimed in claim 1, it is characterized in that, also be provided with temperature probe in described tank body (1) and the interlayer, tank body (1) top also has mechanical defoaming device (6), mechanical defoaming device (6) is communicated with venting port (8), the foam probe (13) that is communicated with mechanical defoaming device (6) is housed in the venting port (8), and liquidometer (11) and control panel (5) are equipped with in the side of tank body (1), and control panel (5) is communicated with described temperature probe, air regulator.
3. fruit vinegar fermentor tank as claimed in claim 1 or 2, it is characterized in that, described inlet system (3) is arranged on impeller pump (2) and the rising pipe that tank body (1) is connected, promptly at the vertical airway (101) that inserts on the inlet system (3) in the 10cm～20cm place of distance mouth spray (102), airway (101) insertion end is 30 ° of angles, angle faces water (flow) direction, and the caliber ratio of rising pipe and airway (101) is no more than 1: 0.5.
4. fruit vinegar fermentor tank as claimed in claim 1 or 2 is characterized in that, described injection system (4) is one tunnel air inlet multichannel shower nozzle, or multichannel air inlet multichannel shower nozzle, and injection direction is that the inwall of shower nozzle and tank body (1) is tangential direction.
5. fruit vinegar fermentor tank as claimed in claim 5 is characterized in that, described one tunnel air inlet multichannel shower nozzle is connected in vertical direction with tank body (1) inwall.
6. fruit vinegar fermentor tank as claimed in claim 1 is characterized in that, the inlet pipe of described inlet system (3) also is connected with the digital display air regulator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101051612A CN100487103C (en) | 2006-12-14 | 2006-12-14 | Fruit vinegar fermenting tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101051612A CN100487103C (en) | 2006-12-14 | 2006-12-14 | Fruit vinegar fermenting tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101020887A true CN101020887A (en) | 2007-08-22 |
| CN100487103C CN100487103C (en) | 2009-05-13 |
Family
ID=38708763
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006101051612A Expired - Fee Related CN100487103C (en) | 2006-12-14 | 2006-12-14 | Fruit vinegar fermenting tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100487103C (en) |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101880624A (en) * | 2010-06-18 | 2010-11-10 | 河南省林业学校 | Method for brewing fruit vinegar from almond-apricot pulp |
| CN101709263B (en) * | 2009-10-30 | 2012-07-18 | 南京工业大学 | Chemostat continuous cultivation device |
| CN102994315A (en) * | 2012-12-18 | 2013-03-27 | 苏州麦克食品机械塑胶有限公司 | Wine food processing device |
| CN104707523A (en) * | 2015-02-17 | 2015-06-17 | 无锡昊瑜节能环保设备有限公司 | Efficient stirring equipment |
| CN105112282A (en) * | 2015-10-15 | 2015-12-02 | 王印江 | Full-automatic drum-type fermentation tank for solid vinegar |
| CN106754296A (en) * | 2016-12-09 | 2017-05-31 | 昆山博青生物科技有限公司 | The installation for fermenting and method of high-efficiency fermenting production bacteriocin |
| CN107118935A (en) * | 2017-05-26 | 2017-09-01 | 河北农业大学 | A kind of family fruit vinegar fermentation machine |
| CN107998992A (en) * | 2017-12-05 | 2018-05-08 | 浙江天奇新材料科技股份有限公司 | A kind of heat cure furane resins are fixed than production system and technique |
| CN108015916A (en) * | 2017-12-05 | 2018-05-11 | 阜阳市金亮涂料有限公司 | Heat cure furane resins compare production technology surely |
| CN108015919A (en) * | 2017-12-05 | 2018-05-11 | 阜阳市金亮涂料有限公司 | A kind of highly effective continuous mixture manufacturing technique of resin |
| CN108165455A (en) * | 2018-03-14 | 2018-06-15 | 佛山市三水区嘉华化学研究院（普通合伙） | A kind of circulating kudzu root vinegar installation for fermenting |
| CN108315204A (en) * | 2018-05-08 | 2018-07-24 | 李�远 | A kind of brewing method of Pomegranate vinegar |
| CN108441414A (en) * | 2018-06-21 | 2018-08-24 | 农业部规划设计研究院 | A kind of anaerobic dry fermentation percolate flow behavior test device and test method |
| CN108624434A (en) * | 2018-07-01 | 2018-10-09 | 通化天池葡萄酒有限责任公司 | Wine fermentation tank |
| CN109280606A (en) * | 2017-07-19 | 2019-01-29 | 岐山天缘食品有限公司 | A kind of efficient vinegar liquid state fermentation method for producing acid |
| CN110437968A (en) * | 2019-09-05 | 2019-11-12 | 让古戎生物科技(苏州)有限公司 | A kind of rose vinegar installation for fermenting |
-
2006
- 2006-12-14 CN CNB2006101051612A patent/CN100487103C/en not_active Expired - Fee Related
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101709263B (en) * | 2009-10-30 | 2012-07-18 | 南京工业大学 | Chemostat continuous cultivation device |
| CN101880624A (en) * | 2010-06-18 | 2010-11-10 | 河南省林业学校 | Method for brewing fruit vinegar from almond-apricot pulp |
| CN102994315A (en) * | 2012-12-18 | 2013-03-27 | 苏州麦克食品机械塑胶有限公司 | Wine food processing device |
| CN104707523A (en) * | 2015-02-17 | 2015-06-17 | 无锡昊瑜节能环保设备有限公司 | Efficient stirring equipment |
| CN105112282A (en) * | 2015-10-15 | 2015-12-02 | 王印江 | Full-automatic drum-type fermentation tank for solid vinegar |
| CN105112282B (en) * | 2015-10-15 | 2018-01-26 | 王印江 | Full automatic drum type solid-state vinegar fermentation tank |
| CN106754296A (en) * | 2016-12-09 | 2017-05-31 | 昆山博青生物科技有限公司 | The installation for fermenting and method of high-efficiency fermenting production bacteriocin |
| CN106754296B (en) * | 2016-12-09 | 2019-06-21 | 昆山博青生物科技有限公司 | The installation for fermenting and method of high-efficiency fermenting production bacteriocin |
| CN107118935A (en) * | 2017-05-26 | 2017-09-01 | 河北农业大学 | A kind of family fruit vinegar fermentation machine |
| CN109280606A (en) * | 2017-07-19 | 2019-01-29 | 岐山天缘食品有限公司 | A kind of efficient vinegar liquid state fermentation method for producing acid |
| CN108015919A (en) * | 2017-12-05 | 2018-05-11 | 阜阳市金亮涂料有限公司 | A kind of highly effective continuous mixture manufacturing technique of resin |
| CN108015916A (en) * | 2017-12-05 | 2018-05-11 | 阜阳市金亮涂料有限公司 | Heat cure furane resins compare production technology surely |
| CN107998992A (en) * | 2017-12-05 | 2018-05-08 | 浙江天奇新材料科技股份有限公司 | A kind of heat cure furane resins are fixed than production system and technique |
| CN107998992B (en) * | 2017-12-05 | 2020-04-28 | 浙江天奇新材料科技股份有限公司 | Hot-curing furan resin fixed-ratio production system and process |
| CN108165455A (en) * | 2018-03-14 | 2018-06-15 | 佛山市三水区嘉华化学研究院（普通合伙） | A kind of circulating kudzu root vinegar installation for fermenting |
| CN108315204A (en) * | 2018-05-08 | 2018-07-24 | 李�远 | A kind of brewing method of Pomegranate vinegar |
| CN108441414A (en) * | 2018-06-21 | 2018-08-24 | 农业部规划设计研究院 | A kind of anaerobic dry fermentation percolate flow behavior test device and test method |
| CN108441414B (en) * | 2018-06-21 | 2023-11-17 | 农业部规划设计研究院 | Device and method for testing flow characteristics of anaerobic dry fermentation percolate |
| CN108624434A (en) * | 2018-07-01 | 2018-10-09 | 通化天池葡萄酒有限责任公司 | Wine fermentation tank |
| CN110437968A (en) * | 2019-09-05 | 2019-11-12 | 让古戎生物科技(苏州)有限公司 | A kind of rose vinegar installation for fermenting |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100487103C (en) | 2009-05-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100487103C (en) | Fruit vinegar fermenting tank | |
| CN102350256B (en) | Micro-nano bubble generating device, and fermentation apparatus and fermentation method using same | |
| CN202107697U (en) | Swirling flow airlift fermentation tank | |
| CN201850276U (en) | Micro-filtration membrane coupling high-density culture device for lactic acid bacteria | |
| CN102796650A (en) | Cyclone airlift fermentation tank | |
| CN101538532B (en) | External loop air lift type membrane bioreactor | |
| CN201313899Y (en) | Novel circulating packed bed reactor | |
| CN208362212U (en) | A kind of composite microbiological fertilizer fermentor | |
| CN210394377U (en) | Anaerobe culture system | |
| CN108441416A (en) | A kind of static fermentation device and its fermentation process and application | |
| CN2483394Y (en) | Solid substrate fermantation tank | |
| RU2236451C1 (en) | Aerobic liquid phase fermentation apparatus | |
| CN2334762Y (en) | High oxygen solubility ferment pot | |
| CN201834919U (en) | Horizontal mixing bioreactor | |
| CN108359588B (en) | Photosynthetic culture fermentation tank | |
| CN209468432U (en) | A kind of gas lift circulation fermentation pot | |
| CN101397538B (en) | Novel circulation-type packed bed reactor | |
| CN203807476U (en) | Fermentation tank | |
| CN201598284U (en) | Efficient and energy-saving antibiotic fermentation tank | |
| CN108330064A (en) | Solid material continuous sterilization and Zymolysis Equipment and continuous sterilization and fermentation system | |
| CN201506790U (en) | Fermentation tank | |
| CN208815005U (en) | A kind of Horizontal type solid fermentation device | |
| CN207079239U (en) | Solid state fermentation system | |
| CN2813623Y (en) | Multi-tube external circulating reactor | |
| CN2078322U (en) | Air-lift biological reactor for high-visco sity fermentation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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: 20090513 Termination date: 20100114 |