CN203530320U - Equipment for logarithmic proliferation fermentation - Google Patents
Equipment for logarithmic proliferation fermentation Download PDFInfo
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- CN203530320U CN203530320U CN201320634838.7U CN201320634838U CN203530320U CN 203530320 U CN203530320 U CN 203530320U CN 201320634838 U CN201320634838 U CN 201320634838U CN 203530320 U CN203530320 U CN 203530320U
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Abstract
The utility model discloses equipment for logarithmic proliferation fermentation. The equipment comprises a fermenting tank body and a base, wherein the base is connected to the bottom part of the fermenting tank body through a hollow-out supporting frame; an automatic frequency conversion device is arranged on one side of the fermenting tank body and used for controlling the revolving speed and operation time of a motor on the fermenting tank body; an upper cover, a motor, a pressure gauge and a ventilating valve are arranged on the top of the fermenting tank body; a baffle plate is arranged in the upper cover; an agitator connected with the motor is arranged in the fermenting tank body; a venturi tube connected with a water inlet and an inlet gas source is arranged on the fermenting tank body; a temperature sensor is arranged on the side edge of the fermenting tank body; the base comprises a heating water tank, and a heating device arranged below the heating water tank; a water inlet hole, a draining hole and an observing pipe are formed and arranged on the heating water tank. With the adoption of the equipment, coacervate bacterial colony produced by the proliferation of microorganism can be decomposed, ageing and spore production can be avoided, and ripening fermentation is accelerated.
Description
Technical field
The utility model relates to a kind of fermentation equipment, more detailed, refers to especially a kind of equipment of logarithm hyperplasia fermentation.
Background technology
Microorganism completes life cycle with spore, logarithm division and proliferation, maturation, old and feeble quadravalence section; Need the nutrition of water, oxygen and miniaturization through enzymatic conversion, generate 2 ATP(bioenergys), organic life entity of could regenerative cell recombinating.
We are called fermentation by microbe application in food-processing, common as wine, fruit vinegar etc., and traditional zymotic method is solid state fermentation, and the fermentation initial stage needs regularly be stirred; Developed into afterwards liquid state fermentation, through constantly stirring, accelerate fermenting speed, but microorganism completes life cycle with spore, logarithm division and proliferation, maturation, old and feeble quadravalence section, spore must be through just entering logarithmic phase division and proliferation after a while in the process of growing up, and must could drive by water, so, at division and proliferation, can produce bacterium colony presents agglomeration and enters maturation, old and feeble producing the spore phase; Fermentation time need be through N life cycle, and fermentation time cannot shorten.
Utility model content
The technical problem mainly solving of the present utility model be for by untie microorganism reunion bacterium colony, allow ultra micro food and microorganism homogeneous simultaneously, and create eugenic environment and synchronously manufacture hyperoxia micromolecular water; So microorganism, often in the logarithm division and proliferation phase, is accelerated the equipment of fermentation.
The equipment of logarithm hyperplasia fermentation described in the utility model, it consists predominantly of: a fermenter main body and a base that is connected in described fermenter main body via hollow out bracing frame, and described fermenter main body one side is provided with an automatic frequency-conversion device.
The tensimeter and one that described fermenter main body top is provided with upper cover, a motor, the described fermenter main body internal pressure of a measurement arranges the vent valve of gas in fermenter main body, wherein said upper cover contains a baffle plate, and described motor is connected with the agitator being arranged in fermenter main body, described fermenter main body top is provided with a Venturi meter, on described Venturi meter, be connected to a water inlet, an air inlet source, described water inlet is to be connected with the water outlet of fermenter bottom part body via pipe connecting, and described fermenter main body side is provided with temperature inductor.
Described base includes a heating water tank and is arranged on the heating unit of described heating water tank below, establishes a prosopyle, a water vent and sighting tube in described heating water tank.
Described automatic frequency-conversion device is to control motor rotary speed and the runtime of setting in fermenter main body.
Wherein, described fermenter main body and heating water tank are that stainless steel is made, and the upper cover of described fermenter main body, motor, tensimeter, vent valve, Venturi meter, water outlet, temperature inductor and base are all adopted antirust processing; And described heating unit can be to be electric heating heating or gas heating; And the air inlet source of described Venturi meter is mainly input high pressure uncontaminated air.
Accordingly, the utility model is that water and ultra micro food powders are put into fermenter main body via being uniformly mixed into food carbohydrate liquid, and in whipping process, utilize the heating of heating unit water proof simultaneously, in fermenter main body, temperature reaches 61-65 degree and maintains the time of 2 hours, make the saccharification of food carbohydrate liquid, in fermenter main body, temperature is down to 25-30 while spending, utilize upper cover to add microorganism required while fermenting, now the air inlet source phases-time conveying high-pressure uncontaminated air of Venturi meter has together high-speed impact of the food carbohydrate liquid of microorganism with joining, now in water, microbe colony scatters because of shock, and homogenize with food powders, and water is isolated can not reunite and is reduced to general water thereby formation hyperoxia micromolecular water via clashing into granular in high pressure uncontaminated air, accelerate microbial transformation, shorten the ultra micro food powders fermentation maturation time.
The utlity model has following advantage:
The equipment of logarithm hyperplasia fermentation described in the utility model, can make the saturation density of the contained bacterial classification of ultra micro food powders after having fermented reach 10
9individual/more than cubic centimeter, to make microorganism automatically enter resting stage and stop growing, effectively by the state of bacterial classification often in logarithmic phase (i.e. the strongst period);
The equipment of logarithm hyperplasia fermentation described in the utility model, can utilize the utility model effectively to shorten the time of having fermented in liquid fertilizer technique, drinks technique;
The equipment of logarithm hyperplasia fermentation described in the utility model, can untie the reunion bacterium colony that microorganism produces when division and proliferation, avoids aging product spore phenomenon, accelerates maturation fermentation.
Accompanying drawing explanation
Fig. 1 is the equipment front perspective view of logarithm hyperplasia fermentation;
Fig. 2 is the equipment vertical view of logarithm hyperplasia fermentation.
Description of symbols in figure:
1-fermenter main body;
10-upper cover;
11-motor;
110-agitator;
12-tensimeter;
13-vent valve;
14-Venturi meter;
141-air inlet source;
142-water inlet;
143-pipe connecting;
15-temperature-sensitive sticker;
16-baffle plate;
17-water outlet;
2-base;
20-hollow out bracing frame;
21-heating water tank;
210-prosopyle;
211-sighting tube;
212-water vent;
22-heating unit;
3-automatic frequency-conversion device.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail, so that those skilled in the art can better understand the utility model being implemented, but illustrated embodiment is not as to restriction of the present utility model.
First, please refer to Fig. 1 and Fig. 2; As seen from the figure, the equipment of logarithm hyperplasia fermentation described in the utility model, consist predominantly of: a fermenter main body 1 and a base 2 that is connected in described fermenter main body 1 bottom via hollow out bracing frame 20, and described fermenter main body 1 one sides arrange an automatic frequency-conversion device 3; Wherein,
Fermenter main body 1, described fermenter main body 1 top is provided with upper cover 10, one motor 11, one tensimeter 12 and of measuring described fermenter main body 1 internal pressure arranges the vent valve 13 of fermenter main body 1 interior gas, wherein said upper cover 10 contains a baffle plate 16, and described motor 11 is connected with the agitator 110 being arranged in fermenter main body 1, described fermenter main body 1 top is provided with a Venturi meter 14, on described Venturi meter 14, be connected to a water inlet 142 and an air inlet source 141, described water inlet 142 is to be connected with the water outlet 17 of fermenter main body 1 bottom via pipe connecting 143, described fermenter main body 1 side is provided with temperature inductor 15,
Automatic frequency-conversion device 3, described automatic frequency-conversion device 3 is to control motor 11 rotating speeds and the runtime of setting in fermenter main body 1.
When the utility model is implemented, mainly that water and ultra micro food powders are put into fermenter main body 1 via automatic frequency-conversion device 3 control motor 11 rotating mixers 110, speed governing stirs and forms food carbohydrate liquid, and water and ultra micro food powders can be used the heating unit 22 in the base 2 that is connected in described fermenter main body 1 via hollow out bracing frame 20 that the food carbohydrate liquid in fermenter main body 1 is heated to saccharification by heating water tank 21 water proofs at stirring formation food carbohydrate liquid simultaneously, in heat-processed, fermenter main body 1 top is provided with a vent valve 13 and can arranges the interior unnecessary gas of fermenter main body 1, when being heated to tensimeter 12 and temperature-sensitive sticker 15 displays temperatures, reaching 61-65 degree and maintain the time of 2 hours, make the saccharification of food carbohydrate liquid, and can observe via sighting tube 211 content of heating water tank 21 interior water in heating saccharifying, prosopyle 210 that can be heating water tank 21 and water vent 212 regulate the number of heating water tank 21 interior water.
The above, after the saccharification of food carbohydrate liquid, when the interior temperature of fermenter main body 1 is down to the temperature that is applicable to bacterial classification existence, just can add microorganism from upper cover 10, after adding microorganism, with speed governing, be uniformly mixed again with food carbohydrate liquid, air inlet source 141 in the process stirring on Venturi meter 14 can be with interim time conveying high-pressure uncontaminated air to fermenter main body 1, in water inlet 142 meetings of Venturi meter 14 simultaneously of conveying high-pressure uncontaminated air, produce negative pressure, food carbohydrate liquid in fermenter main body 1 is sucked from the water inlet 142 of Venturi meter 14 via the pipe connecting 143 that connects water outlet 17, now food carbohydrate liquid and high pressure uncontaminated air are in conjunction with sending into fermenter main body 1 inner impact baffle plate 16, when empty G&W can present vaporization cigarette shape by nanometer through clashing into later at the interior part water of fermenter main body 1, water molecules after dispersion can not reunited back and form containing hyperoxia micromolecular water because of hyperbaric oxygen, and conveying high-pressure uncontaminated air also can be continued in the air inlet source 141 of Venturi meter 14, the food carbohydrate liquid and the high pressure uncontaminated air that make Venturi meter 14 suck interpolation microorganism from water inlet 142 are together sent into fermenter main body 1 inner impact baffle plate 16, food carbohydrate liquid now, high pressure uncontaminated air, microorganism is because of the continuous homogeneous dispersion of shock, accelerate the time that microbial transformation and fermentation complete.
Accordingly, microorganism in the process of clashing into always in logarithmic phase division and proliferation, the microorganism of division and proliferation, high pressure uncontaminated air and the continuous granular of food carbohydrate fluid molecule, make microorganism can not produce agglomeration, avoid aging product spore phenomenon, allow ultra micro food and microorganism homogeneous simultaneously, accelerate the time that microbial transformation and fermentation complete.
The above embodiment is only the preferred embodiment for absolutely proving that the utility model is lifted, and protection domain of the present utility model is not limited to this.Being equal to that those skilled in the art do on the utility model basis substitutes or conversion, all within protection domain of the present utility model.Protection domain of the present utility model is as the criterion with claims.
Claims (3)
1. the equipment of logarithm hyperplasia fermentation, it is characterized in that, include: a fermenter main body and a base that is connected in described fermenter bottom part body via hollow out bracing frame, described fermenter main body one side arranges the rotating speed of the motor on a controlled fermentation groove body and the automatic frequency-conversion device of runtime, wherein
The tensimeter and one that described fermenter main body top is provided with upper cover, a motor, the described fermenter main body internal pressure of a measurement arranges the vent valve of gas in fermenter main body, described upper cover contains a baffle plate, described motor is connected with the agitator being arranged in fermenter main body, described fermenter main body top is provided with a Venturi meter, on described Venturi meter, be connected to a water inlet, an air inlet source, described water inlet is to be connected with the water outlet of fermenter bottom part body via pipe connecting, and described fermenter main body side is provided with temperature inductor again;
Described base includes a heating water tank and is arranged on the heating unit of described heating water tank below, establishes a prosopyle, a water vent and sighting tube in described heating water tank.
2. the equipment that logarithm hyperplasia is fermented as claimed in claim 1, is characterized in that, described fermenter main body and heating water tank are stainless steel.
3. the equipment that logarithm hyperplasia is fermented as claimed in claim 1, is characterized in that, heating unit is electric heating heating unit or gas heating unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320634838.7U CN203530320U (en) | 2013-10-15 | 2013-10-15 | Equipment for logarithmic proliferation fermentation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320634838.7U CN203530320U (en) | 2013-10-15 | 2013-10-15 | Equipment for logarithmic proliferation fermentation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203530320U true CN203530320U (en) | 2014-04-09 |
Family
ID=50416553
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320634838.7U Expired - Fee Related CN203530320U (en) | 2013-10-15 | 2013-10-15 | Equipment for logarithmic proliferation fermentation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203530320U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104560716A (en) * | 2013-10-15 | 2015-04-29 | 吕胜一 | Logarithmic proliferation fermentation method and device |
| CN109652307A (en) * | 2019-01-28 | 2019-04-19 | 北京狼图腾科技有限公司 | A kind of fermentation tank |
| CN110129183A (en) * | 2019-06-11 | 2019-08-16 | 昆山千亿圆生物科技有限公司 | One kind being evenly heated logarithm fermentation tank |
-
2013
- 2013-10-15 CN CN201320634838.7U patent/CN203530320U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104560716A (en) * | 2013-10-15 | 2015-04-29 | 吕胜一 | Logarithmic proliferation fermentation method and device |
| CN109652307A (en) * | 2019-01-28 | 2019-04-19 | 北京狼图腾科技有限公司 | A kind of fermentation tank |
| CN110129183A (en) * | 2019-06-11 | 2019-08-16 | 昆山千亿圆生物科技有限公司 | One kind being evenly heated logarithm fermentation tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: LIN GUANYIN HUANG QIONGCHENG Free format text: FORMER OWNER: LIN GUANYIN Effective date: 20141114 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20141114 Address after: Taiwan, China Kaohsiung Xinxing District, Wen Road, Lane 25, No. 26 Patentee after: Lv Shengyi Patentee after: Lin Guanyin Patentee after: Huang Qiongcheng Address before: Taiwan, China Kaohsiung Xinxing District, Wen Road, Lane 25, No. 26 Patentee before: Lv Shengyi Patentee before: Lin Guanyin |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140409 Termination date: 20201015 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |