CN204298377U - A kind of high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment - Google Patents
A kind of high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment Download PDFInfo
- Publication number
- CN204298377U CN204298377U CN201420405915.6U CN201420405915U CN204298377U CN 204298377 U CN204298377 U CN 204298377U CN 201420405915 U CN201420405915 U CN 201420405915U CN 204298377 U CN204298377 U CN 204298377U
- Authority
- CN
- China
- Prior art keywords
- tank body
- cooling water
- pipe
- arranges
- efficiency
- 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 - Lifetime
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 94
- 238000000855 fermentation Methods 0.000 title claims abstract description 39
- 230000004151 fermentation Effects 0.000 title claims abstract description 39
- 239000000052 vinegar Substances 0.000 title claims abstract description 34
- 235000021419 vinegar Nutrition 0.000 title claims abstract description 34
- 238000012216 screening Methods 0.000 claims abstract description 43
- 238000001816 cooling Methods 0.000 claims abstract description 38
- 239000000498 cooling water Substances 0.000 claims abstract description 28
- 239000012452 mother liquor Substances 0.000 claims abstract description 28
- 230000001502 supplementing effect Effects 0.000 claims abstract description 16
- 238000001914 filtration Methods 0.000 claims description 26
- 239000006052 feed supplement Substances 0.000 claims description 17
- 239000000706 filtrate Substances 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- 239000007921 spray Substances 0.000 claims description 8
- 239000000523 sample Substances 0.000 claims description 6
- 238000009826 distribution Methods 0.000 claims description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 abstract description 45
- FRXSZNDVFUDTIR-UHFFFAOYSA-N 6-methoxy-1,2,3,4-tetrahydroquinoline Chemical compound N1CCCC2=CC(OC)=CC=C21 FRXSZNDVFUDTIR-UHFFFAOYSA-N 0.000 abstract description 12
- 241000894006 Bacteria Species 0.000 abstract description 11
- 230000011218 segmentation Effects 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- 230000007423 decrease Effects 0.000 abstract description 2
- 238000004513 sizing Methods 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000032683 aging Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000001476 alcoholic effect Effects 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000010413 mother solution Substances 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
- 230000008447 perception Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 210000004243 sweat Anatomy 0.000 description 2
- 238000012935 Averaging Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009295 crossflow filtration Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 230000001256 tonic effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
A kind of high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment, belong to brewery installations field, comprise tank body, cooling pond, mother liquor screening circulation line and wine liquid feed supplementing device, it is characterized in that: in tank body, spiral cooling tube is set, the cooling water pipe that spiral cooling tube one end UNICOM tank body lower part enters, the cooling water pipe that the other end UNICOM tank body top of spiral cooling tube enters; Cooling water pipe UNICOM cooling pond, forms cooling water pipeline; Cooling water pipeline arranges circulating pump and drives cooling water circulation; Tank body lower part arranges mother liquor screening circulation line UNICOM tank interior; Tank body upper end arranges air inlet pipe, arranges wine liquid feed supplementing device in air inlet pipe; The stators and rotators that tank body lower end is arranged in driven by motor tank body rotates.Device structure is reasonable, simple to operate, keeps the step sizing going out vinegar and the strong thalline of acetic acid bacteria continuously, decreases the waste of energy of segmentation interval.
Description
Technical field
The utility model belongs to vinegar and brewages field, is specifically related to a kind of high-efficiency and continuous diaphragm screen and divides self-priming liquid vinegar fermentation equipment.
Background technology
After the seventies, liquid state fermentation legal system vinegar gradually adopts tank fermentation method, starchy material is after liquefaction, saccharification and alcoholic fermentation, distiller's wort is sent in fermentation tank, the acetic acid bacteria liquid that access Pure-culture expands step by step, controls product temperature and ventilation, the oxidation of accelerating alcohol, generate acetic acid, shorten the production cycle.Fermentation tank type is more, now uses self-suction fermentor, and first it produced for vinegar in the initial stage fifties by Germany, is called Frings apparatus for acetic acid fermentation tank, and obtains patent in 1969 years.Japanese, European all states adopt in succession, and China brings into use the seventies.
In liquid submerged fermentation vinegar production process, the split plot design of many employing 3/4-1/2, when each acetic acid rises to production requirement acidity, the vinegar liquid of segmentation 3/4-1/2, residue is as lower batch of seeding, fill into the wine liquid of 3/4-1/2, proceed fermenting and producing, this is the semi continuous mode of production, for domestic most enterprise takes, but this kind of method also existing defects: the first, just segmented because acetic acid bacteria will rise in value in 4 hours, rate of producing acid only has normal 50%, causes energy waste; The second, easily there is aging phenomenon in bacterial classification length service time, causes rate of producing acid to reduce.
In order to overcome the deficiencies in the prior art, my company is in production practices, and high-new membrane filtration technique is applied in liquid deep layer acetic fermentation process, and designed, designed is produced a set of high-efficiency and continuous diaphragm screen and divided self-priming liquid vinegar fermentation system.
Utility model content
Technical problem to be solved in the utility model is, provides a kind of high-efficiency and continuous diaphragm screen to divide self-priming liquid vinegar fermentation equipment, reaches the object of liquid vinegar high-efficiency and continuous fermentation.
The utility model solves the technical scheme that its technical problem adopts: provide a kind of high-efficiency and continuous diaphragm screen to divide self-priming liquid vinegar fermentation instrument and supplies, comprise tank body, cooling pond, mother liquor screening circulation line and wine liquid feed supplementing device, it is characterized in that: in tank body, spiral cooling tube is set, the cooling water pipe that spiral cooling tube one end UNICOM tank body lower part enters, the cooling water pipe that the other end UNICOM tank body top of spiral cooling tube enters; Cooling water pipe UNICOM cooling pond, forms cooling water pipeline; Cooling water pipeline arranges circulating pump and drives cooling water circulation; Tank body lower part arranges mother liquor screening circulation line UNICOM tank interior; Tank body upper end arranges air inlet pipe, arranges wine liquid feed supplementing device in air inlet pipe; The stators and rotators that tank body lower end is arranged in driven by motor tank body rotates.
Mother liquor screening circulation line comprises circulating pump and filtering cabin, and mother liquor screening circulation line is driven by circulating pump, draws, refill in tank body after filtering cabin filters by logical for the liquid in tank body; Arrange in filtering cabin and consider thing outlet, the liquid of filtering is deviate from.
Filtering cabin comprises screening film group, sensor mounting layer, slideway and lift block, the inwall of filtering cabin both sides offers slideway, arranges lift block in slideway, and screening film group is inlaid in slideway, and screening film group is driven by lift block and is elevated; Below screening film group, sensor mounting layer is set; In sensor mounting layer, pressure sensor is set.
Screening film group comprises considers film pipe, worry hole and filtrate (liquid, arranges the worry film pipe of more than two in screening film, considers array distribution on film pipe and considers hole; Consider film pipe by Lv Kong UNICOM filtrate (liquid.
The aperture of considering hole is 0.4-0.45 micron.
Wine liquid feed supplementing device comprises wine liquid feed supplement pipe and atomizing spray head, and wine liquid feed supplement pipe one end is stretched in air inlet pipe, arranges atomizing spray head at port, and the other end of wine liquid feed supplement pipe connects wine liquid feed supplement tank.
Tank body arranges temperature probe and alcohol probe.
The beneficial effects of the utility model are:
1, liquid vinegar fermentation system described in the utility model, arranges spiral cooling tube in tank body, for reducing the heat energy that sweat in tank body produces.Spiral cooling tube one end enters from tank body lower part, and the other end passes from tank body top, runs through whole tank body, makes radiating effect more efficient and stable.The cooling pond that spiral cooling tube will be discharged to after the heat absorption in tank body outside tank body, is carried out cooling down, then is entered by the other end of spiral cooling tube, be injected into the spiral cooling tube in tank body by circulating pump, forms cooling water pipeline.Tank body lower part is provided with mother liquor screening circulation line, carries out filtration deviate from mother liquor.Tank body upper end is provided with air inlet pipe, makes air can participate in liquid vinegar fermentation process, and is arranged with pipe by wine liquid feed supplementing device.Device structure is reasonable, simple to operate, keeps the step sizing going out vinegar and the strong thalline of acetic acid bacteria continuously, decreases the waste of energy of segmentation interval.
2, mother liquor screening circulation line is driven by circulating pump, is drawn by the liquid mother of vinegar liquid in tank body, and deviate from the materials such as vinegar liquid, acetic acid bacteria deformity thalline, dead thalline through filtering cabin screening, strong acetic acid bacteria thalline refills in tank body with mother liquor, participates in fermentation.Mother liquor efficient fermentation efficiency can be kept the moment.
The inwall of the filtering cabin both sides 3, in equipment offers slideway, and screening film group is inlaid in slideway, arranges sensor mounting layer below screening film group, by arranging pressure sensor in sensor mounting layer, and the weight of sensing screening film group.When screening film group in the course of the work, occur damaging or aging after, the weight of screening film group can change, and after pressure sensor perception, starts the lift block in slideway, screening film group is promoted from filtering cabin, facilitate Timeliness coverage and replacing.Embody the automation of equipment on the one hand, the moment maintains the steady quality of product on the other hand.
4, described wine liquid feed supplementing device, stretches in air inlet pipe by direct wine liquid feed supplement pipe, arranges atomizing spray head at port.Wine liquid enters fermentation tank by air inlet pipe after being atomized by atomizer, and through rotor, stator high speed dispersion in zymotic fluid, ensure that wine liquid can moment and original fermentation liquor mix.
5, liquid vinegar fermentation technique described in the utility model, comprise three processing steps, successively through acetic fermentation step, diaphragm screen step by step with feed supplement step, first in tank, configure required liquid vinegar fermentation liquid, then open mother liquor screening circulation line and wine liquid feed supplementing device simultaneously, synchronously carry out diaphragm screen step by step with feed supplement step, diaphragm screen step by step in from mother liquor, deviate from vinegar liquid, acetic acid bacteria deformity thalline, dead thalline etc., the wine liquid feed supplementing device of synchronous averaging can supplement the mother liquor of disappearance timely, maintains the continuity of liquid vinegar fermentation work.
6, the utility model is suitable for practicality, and production cost is lower, is suitable in the industry cycle popularizing.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is that the A of filtering cabin in Fig. 1 is to structural representation;
Fig. 3 is the enlarged drawing of wine liquid feed supplementing device, i.e. the B portion partial enlarged drawing of Fig. 1;
Fig. 4 is the operation principle schematic diagram of filtering cabin;
In figure: 1, tank body; 2, cooling water pipe; 3, cooling pond; 4, circulating pump; 5, motor; 6. Recycling Mother Solution pipeline; 7, circulating pump; 8, filtering cabin; 9, filtrate (liquid; 10, spiral cooling tube; 11, air inlet pipe; 12, wine liquid feed supplementing device; 13, wine liquid feed supplement pipe; 14, sensor mounting layer; 15, pressure sensor; 16, lift block; 17, film group is sieved; 18, atomizer; 19, film pipe is considered; 20, hole is considered; 21, filtrate (liquid.
Detailed description of the invention
Below in conjunction with accompanying drawing and detailed description of the invention, the utility model is described in further detail.
As shown in Figure 1, spiral cooling tube 10 is set, for reducing the heat energy that sweat in tank body produces in tank body 1.Spiral cooling tube 10 runs through whole tank body from top to bottom in tank body 1, makes radiating effect more efficient and stable.The cooling water pipe 2 that UNICOM's tank body 1 bottom, spiral cooling tube 10 one end enters, the cooling water pipe 2 that other end UNICOM tank body 1 top of spiral cooling tube 10 enters; Cooling water pipe 2 UNICOM cooling pond 3, forms cooling water pipeline.Spiral cooling tube 10, by cooling water pipe 2, after the heat absorption in tank 1, is discharged to cooling pond 3 and carries out cooling down, then entered by the other end of cooling water pipe 2, be injected into the spiral cooling tube 10 in tank body 1 by circulating pump 4.Tank body 1 bottom is provided with mother liquor screening circulation line 6, carries out filtration deviate from mother liquor.
As shown in Figure 2, mother liquor screening circulation line 6 is driven by circulating pump 7, is drawn by the liquid in tank body 1, refills in tank body 1 after filtering cabin 8 filters.The inwall of filtering cabin 8 both sides offers slideway, arrange lift block 16 in slideway, screening film group 17 is inlaid in slideway, arranges sensor mounting layer 14 below screening film group 17, by arranging pressure sensor 15 in sensor mounting layer 14, the weight of sensing screening film group 17.When screening film group 17 in the course of the work, occur damaging or aging after, the weight of screening film group 17 can change, and after pressure sensor 15 perception, starts the lift block 16 in slideway, screening film group 17 is promoted from filtering cabin 8.Arrange in filtering cabin 8 and consider thing outlet 9, the liquid of filtering is deviate from.
Tank body 1 upper end is provided with air inlet pipe 11, makes air can participate in liquid vinegar fermentation process, and is arranged with pipe by wine liquid feed supplementing device 12.As shown in Figure 3, wine liquid feed supplement pipe 13 one end is stretched in air inlet pipe 11, arranges atomizing spray head 18 at port, and the other end of wine liquid feed supplement pipe 13 connects wine liquid feed supplement tank.Wine liquid enters fermentation tank by air inlet pipe 11 after being atomized by atomizer 18, and through rotor, stator high speed dispersion in zymotic fluid, ensure that wine liquid can moment and original fermentation liquor mix.
As shown in Figure 4, mother liquor stream is when screening film group 17, and mother liquor enters filter membrane pipe 19 along liquid-transport pipe-line, and filter vinegar liquid, acetic acid bacteria deformity thalline, dead thalline etc. by considering hole 20, the liquid leached is deviate from by filtrate (liquid 21.
Work of the present utility model is omnidistance as follows:
Wine liquid is mixed with standard wine liquid 7-10%, is delivered to atomizer 18 by wine liquid feed supplement pipe 13, the atomization of wine liquid sprays in air inlet pipe 11 by atomizer 18, enters tank body 1 by air inlet pipe 11.Open cooling and follow bad pipeline, spiral cooling tube 10, by cooling water pipe 2, after the heat absorption in tank 1, is discharged to cooling pond 3 and carries out cooling down, then entered by the other end of cooling water pipe 2, be injected into the spiral cooling tube 10 in tank body 1 by circulating pump 4.Add 10% seeding tank bacterial classification, the total coefficient 70-80% of fermentation tank.Start the acetic fermentation stage, operating temperature controls at 29 to 31 degrees Celsius.Total acid rises gradually, can detect zymotic fluid residual alcohol content with alcohol probe, when residual wine reaches 0.1%, opens mother liquor screening circulation line 6 and wine liquid feed supplementing device 12 simultaneously.Mother liquor screening circulation line 6 is driven by circulating pump 7, liquid in tank body 1 is drawn, through filtering cabin 8, mother liquor enters filter membrane pipe 19 along liquid-transport pipe-line, during by considering hole 20, adopt the microfiltration membranes of 0.4-0.45 micron pore size, adopt cross-flow filtration method, filter vinegar liquid, acetic acid bacteria deformity thalline, dead thalline and other granular sizes and be less than 0.4-0.45 micron composition, the liquid leached enters filtrate (liquid 9 by filtrate (liquid 21 and deviates from, the strong thalline size of acetic acid bacteria, at 0.6 × 2 ~ 3 microns, not by fenestra, flows back to tank body 1 by Recycling Mother Solution pipeline 6.
The part that mother liquor is deviate from, is supplemented by automatic tonic wine liquid system, by alcohol probes sense, controls alcoholic strength and remains in 0.1 ± 0.02% scope, namely adds the amount of alcohol and acetic acid bacteria in the unit interval and transforms alcohol to become the amount of acetic acid equal.Wine liquid is delivered to atomizer 18 by wine liquid feed supplement pipe 13, the atomization of wine liquid sprays in air inlet pipe 11 by atomizer 18, enter tank body 1 by air inlet pipe 11, give to supplement timely to the mother liquor of tank body 1 internal loss, be convenient to the fermentation work that continuous print completes liquid vinegar.
It is to be noted; above-mentioned embodiment is only the utility model preferred embodiment; for those skilled in the art, under the prerequisite meeting utility model works principle, any equivalent or similar replacement all falls in protection domain of the present utility model.
Claims (7)
1. a high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment, comprise tank body, cooling pond, mother liquor screening circulation line and wine liquid feed supplementing device, it is characterized in that: in tank body, spiral cooling tube is set, the cooling water pipe that spiral cooling tube one end UNICOM tank body lower part enters, the cooling water pipe that the other end UNICOM tank body top of spiral cooling tube enters; Cooling water pipe UNICOM cooling pond, forms cooling water pipeline; Cooling water pipeline arranges circulating pump and drives cooling water circulation; Tank body lower part arranges mother liquor screening circulation line UNICOM tank interior; Tank body upper end arranges air inlet pipe, arranges wine liquid feed supplementing device in air inlet pipe; The stators and rotators that tank body lower end is arranged in driven by motor tank body rotates.
2. a kind of high-efficiency and continuous diaphragm screen according to claim 1 divides self-priming liquid vinegar fermentation equipment, it is characterized in that: mother liquor screening circulation line comprises circulating pump and filtering cabin, mother liquor screening circulation line is driven by circulating pump, liquid in tank body is drawn, refills in tank body after filtering cabin filters; Arrange in filtering cabin and consider thing outlet, the liquid of filtering is deviate from.
3. a kind of high-efficiency and continuous diaphragm screen according to claim 2 divides self-priming liquid vinegar fermentation equipment, it is characterized in that: filtering cabin comprises screening film group, sensor mounting layer, slideway and lift block, the inwall of filtering cabin both sides offers slideway, in slideway, lift block is set, screening film group is inlaid in slideway, and screening film group is driven by lift block and is elevated; Below screening film group, sensor mounting layer is set; In sensor mounting layer, pressure sensor is set.
4. a kind of high-efficiency and continuous diaphragm screen according to claim 3 divides self-priming liquid vinegar fermentation equipment, it is characterized in that: screening film group comprises considers film pipe, worry hole and filtrate (liquid, arranges the worry film pipe of more than two in screening film, considers array distribution on film pipe and considers hole; Consider film pipe by Lv Kong UNICOM filtrate (liquid.
5. a kind of high-efficiency and continuous diaphragm screen according to claim 4 divides self-priming liquid vinegar fermentation equipment, it is characterized in that: the aperture of considering hole is 0.4-0.45 micron.
6. a kind of high-efficiency and continuous diaphragm screen according to claim 1 divides self-priming liquid vinegar fermentation equipment, it is characterized in that: wine liquid feed supplementing device comprises wine liquid feed supplement pipe and atomizing spray head, wine liquid feed supplement pipe one end is stretched in air inlet pipe, arrange atomizing spray head at port, the other end of wine liquid feed supplement pipe connects wine liquid feed supplement tank.
7. a kind of high-efficiency and continuous diaphragm screen according to claim 1 divides self-priming liquid vinegar fermentation equipment, it is characterized in that: tank body arranges temperature probe and alcohol probe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420405915.6U CN204298377U (en) | 2014-07-15 | 2014-07-15 | A kind of high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420405915.6U CN204298377U (en) | 2014-07-15 | 2014-07-15 | A kind of high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204298377U true CN204298377U (en) | 2015-04-29 |
Family
ID=53103934
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420405915.6U Expired - Lifetime CN204298377U (en) | 2014-07-15 | 2014-07-15 | A kind of high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204298377U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105608629A (en) * | 2015-12-24 | 2016-05-25 | 杨德太 | Ecological organic fertilizer industrial park |
| CN106580069A (en) * | 2016-12-22 | 2017-04-26 | 厦门升久实业有限公司 | Pipeline-type intelligent steam machine |
-
2014
- 2014-07-15 CN CN201420405915.6U patent/CN204298377U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105608629A (en) * | 2015-12-24 | 2016-05-25 | 杨德太 | Ecological organic fertilizer industrial park |
| CN106580069A (en) * | 2016-12-22 | 2017-04-26 | 厦门升久实业有限公司 | Pipeline-type intelligent steam machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204400998U (en) | A kind of novel microbial ferment device | |
| CN206553499U (en) | A kind of vinegar produces installation for fermenting | |
| CN105273973B (en) | A kind of high-efficiency and continuous diaphragm screen point self-priming liquid vinegar fermentation equipment and technique | |
| CN204298377U (en) | A kind of high-efficiency and continuous diaphragm screen divides self-priming liquid vinegar fermentation equipment | |
| CN205088244U (en) | Horizontal liquid state fermentation jar fire fighting equipment | |
| CN203976796U (en) | Biological fermentation tank with separated foamite system | |
| CN204125452U (en) | Multistage continuous fermentation device | |
| CN203144387U (en) | Automatic feeding and continuous circulation device for fungus liquid for fermenting vegetables | |
| CN103666900A (en) | Tandem-type fermentor group and use method thereof | |
| CN203625373U (en) | Batch culture tank | |
| CN103014071B (en) | Preparation method for producing high-concentration marsh gas and production device thereof | |
| CN205893245U (en) | Microbial fermentation tank | |
| CN215103160U (en) | Self-made liquid vinegar fermentation culture medium adding device | |
| CN212476674U (en) | Novel white spirit low-temperature fermentation equipment | |
| CN206219579U (en) | Membrane module, the bioreactor containing the membrane module and Zymolysis Equipment | |
| CN209065876U (en) | A kind of acetic fermentation automatic turning unstrained spirits device | |
| CN106072728A (en) | A kind of probiotics fermentation tank of feed additive | |
| CN218012080U (en) | Energy-saving practical ceramic membrane water-adding dialysis device | |
| CN205062069U (en) | System for produce ethanol with straw | |
| CN214937416U (en) | Fermentation equipment based on membrane extraction separation technology | |
| CN202201904U (en) | Dissolved oxygen control system in high cell density fermentation process | |
| CN212476673U (en) | Automatic temperature control device of white spirit low-temperature fermentation equipment | |
| CN215517377U (en) | Food processing fermenting installation | |
| CN205443238U (en) | Automatic continuous white spirit homogenizing device | |
| CN204727864U (en) | A kind of fermentation unit for alcoholic |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 255300 Shandong province Zhoucun District North Development Zone, silk road, No. 1688 Patentee after: Shandong Yutu food Limited by Share Ltd Address before: 255300 Shandong province Zhoucun District North Development Zone, silk road, No. 1688 Patentee before: Shandong Jade Hare Food Co., Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 255300 Silk Road, Zhoucun Economic Development Zone, Shandong, China, No. 1688, No. Patentee after: Shandong Yutu food Limited by Share Ltd Address before: 255300 Shandong province Zhoucun District North Development Zone, silk road, No. 1688 Patentee before: Shandong Yutu food Limited by Share Ltd |
|
| CP02 | Change in the address of a patent holder |